diff options
author | Sashi20 | 2021-10-01 00:20:13 +0550 |
---|---|---|
committer | Sashi20 | 2021-10-01 00:20:13 +0550 |
commit | c1aefba9014a8511bc65580bdb83c84fd417144e (patch) | |
tree | 360617519456718e32a95bec2877ac360fb8d382 | |
parent | 9d98e10baf94887dd5edb8d4632bc4ced5327620 (diff) | |
download | DWSIM-Flowsheets-c1aefba9014a8511bc65580bdb83c84fd417144e.tar.gz DWSIM-Flowsheets-c1aefba9014a8511bc65580bdb83c84fd417144e.tar.bz2 DWSIM-Flowsheets-c1aefba9014a8511bc65580bdb83c84fd417144e.zip |
Added(A)/Deleted(D) following Flowsheet file
A Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf
A Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Isopropyl_alcohol_synthesis_from_propylene_and_water_adapted.dwxmz
A Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/Flowsheet.dwxmz
A Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/abstract.pdf
A Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Abstract.pdf
A Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxml
A Simulation_And_Optimization_Of_Cyclohexanone_Ammoximation_Process_Over_Ts-1_Catalyst_By_Mr_Dhaval_R_Patel/user_defined_compound/Compound.zip
-rw-r--r-- | Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf | bin | 0 -> 359828 bytes | |||
-rw-r--r-- | Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Isopropyl_alcohol_synthesis_from_propylene_and_water_adapted.dwxmz | bin | 0 -> 432673 bytes | |||
-rw-r--r-- | Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/Flowsheet.dwxmz | bin | 0 -> 166802 bytes | |||
-rw-r--r-- | Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/abstract.pdf | bin | 0 -> 664798 bytes | |||
-rw-r--r-- | Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Abstract.pdf | bin | 0 -> 226588 bytes | |||
-rw-r--r-- | Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxml | 8223 | ||||
-rw-r--r-- | Simulation_And_Optimization_Of_Cyclohexanone_Ammoximation_Process_Over_Ts-1_Catalyst_By_Mr_Dhaval_R_Patel/user_defined_compound/Compound.zip | bin | 0 -> 4529 bytes |
7 files changed, 8223 insertions, 0 deletions
diff --git a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf Binary files differnew file mode 100644 index 0000000..653e0db --- /dev/null +++ b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf diff --git a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Isopropyl_alcohol_synthesis_from_propylene_and_water_adapted.dwxmz b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Isopropyl_alcohol_synthesis_from_propylene_and_water_adapted.dwxmz Binary files differnew file mode 100644 index 0000000..92bd1f4 --- /dev/null +++ b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Isopropyl_alcohol_synthesis_from_propylene_and_water_adapted.dwxmz diff --git a/Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/Flowsheet.dwxmz b/Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/Flowsheet.dwxmz Binary files differnew file mode 100644 index 0000000..858516c --- /dev/null +++ b/Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/Flowsheet.dwxmz diff --git a/Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/abstract.pdf b/Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/abstract.pdf Binary files differnew file mode 100644 index 0000000..9052513 --- /dev/null +++ b/Manufacturing_Of_1,2-Dichloroethane_By_Mr_Mihir_Jain_And_Ms.yashvi_Shah/abstract.pdf diff --git a/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Abstract.pdf b/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Abstract.pdf Binary files differnew file mode 100644 index 0000000..e7f95f4 --- /dev/null +++ b/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Abstract.pdf diff --git a/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxml b/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxml new file mode 100644 index 0000000..517fb52 --- /dev/null +++ b/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxml @@ -0,0 +1,8223 @@ +<?xml version="1.0" encoding="utf-8"?>
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+ <MobileCompatible>true</MobileCompatible>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
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+ <Name>Aqueous</Name>
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>7</ID>
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
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+ <DynamicProperties />
+ </Compound>
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Vessel</Type>
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+ <FlashTemperature>298.15</FlashTemperature>
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+ <ExternalSolverConfigData></ExternalSolverConfigData>
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+ <Calculated>true</Calculated>
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+ <Name>Liquid Level</Name>
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+ <Data>"Current Vessel Operating Pressure"</Data>
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+ <PropertyType>System.String</PropertyType>
+ <Data>"Empties the vessel's content on the next run."</Data>
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+ </DynamicPropertiesDescriptions>
+ <DynamicPropertiesUnitTypes>
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+ <AttachedUtilities />
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+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
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+ <Calculated>true</Calculated>
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+ <DynamicPropertiesUnitTypes />
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+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
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+ <Name2>MAT-5f834b55-1e31-45bb-88d6-23ce170be830</Name2>
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+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Pressure_and_Enthalpy</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
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+ <DynamicsOnly>false</DynamicsOnly>
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+ <Calculated>true</Calculated>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <molar_helmholtz_energy>5651.8246093639</molar_helmholtz_energy>
+ <molar_internal_energy>-8644.41198918081</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
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+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>10000000</PartialPressure>
+ <PartialVolume>0.174593999999954</PartialVolume>
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+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>-Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
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+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Methane</ComponentName>
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+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid1</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid1</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
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+ <kinematic_viscosity>5.51535530518539E-07</kinematic_viscosity>
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+ <molar_entropy>-68.0773171359453</molar_entropy>
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+ <molar_helmholtz_energy>5651.8246093639</molar_helmholtz_energy>
+ <molar_internal_energy>-8644.41198918081</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Methane</ComponentName>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
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+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid2</ComponentName>
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+ <Name>Liquid2</Name>
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+ <Properties>
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+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ComponentName>Liquid3</ComponentName>
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+ <Name>Liquid3</Name>
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+ <Properties>
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+ <gibbs_free_energy>0</gibbs_free_energy>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <ComponentName>Methane</ComponentName>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Aqueous</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Aqueous</Name>
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+ <Properties>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
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+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
+ <ObjectClass>Exchangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
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+ <OutletTemperature>210</OutletTemperature>
+ <OutletVaporFraction>0</OutletVaporFraction>
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+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
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+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
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+ <Kvalue>NaN</Kvalue>
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+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <massflow>0.000277777777777778</massflow>
+ <molar_enthalpy>2558.56053550429</molar_enthalpy>
+ <molar_entropy>-30.0272843716743</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molecularWeight>16.04246</molecularWeight>
+ <pressure>10000000</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>389.231777541323</temperature>
+ <thermalConductivity>0.0477613711106083</thermalConductivity>
+ <volumetric_flow>5.60331249848243E-06</volumetric_flow>
+ <gibbs_free_energy>888.026761870055</gibbs_free_energy>
+ <helmholtz_energy>697.075576088814</helmholtz_energy>
+ <internal_energy>-31.4643903954784</internal_energy>
+ <molar_gibbs_free_energy>14246.1338062299</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>11182.8070463817</molar_helmholtz_energy>
+ <molar_internal_energy>-504.766224343846</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938431055415</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>OverallLiquid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0</compressibilityFactor>
+ <density>NaN</density>
+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>NaN</kinematic_viscosity>
+ <massflow>0</massflow>
+ <massfraction>0</massfraction>
+ <molar_enthalpy>NaN</molar_enthalpy>
+ <molar_entropy>NaN</molar_entropy>
+ <molarflow>0</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>NaN</molecularWeight>
+ <thermalConductivity>0</thermalConductivity>
+ <viscosity>0</viscosity>
+ <volumetric_flow>0</volumetric_flow>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0.0194256323684718</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>3090.16514914883</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>10000000</PartialPressure>
+ <PartialVolume>0.323607299847856</PartialVolume>
+ <VolumetricFlow>5.60331249848243E-06</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>-Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.946618559373772</compressibilityFactor>
+ <density>49.5738507986141</density>
+ <enthalpy>159.486795385763</enthalpy>
+ <entropy>-1.87173814811908</entropy>
+ <heatCapacityCp>2.80252660658518</heatCapacityCp>
+ <heatCapacityCv>1.98204989033583</heatCapacityCv>
+ <jouleThomsonCoefficient>-8.33551787795939E-10</jouleThomsonCoefficient>
+ <kinematic_viscosity>3.09066666678043E-07</kinematic_viscosity>
+ <massflow>0.000277777777777778</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>2558.56053550429</molar_enthalpy>
+ <molar_entropy>-30.0272843716744</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>16.04246</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.0477613711106083</thermalConductivity>
+ <viscosity>1.53216248207223E-05</viscosity>
+ <volumetric_flow>5.60331249848243E-06</volumetric_flow>
+ <bulk_modulus>-5014.26485478046</bulk_modulus>
+ <gibbs_free_energy>888.026761870055</gibbs_free_energy>
+ <helmholtz_energy>697.075576088814</helmholtz_energy>
+ <internal_energy>-31.4643903954784</internal_energy>
+ <isothermal_compressibility>-0.00019943102906633</isothermal_compressibility>
+ <molar_gibbs_free_energy>14246.1338062299</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>11182.8070463817</molar_helmholtz_energy>
+ <molar_internal_energy>-504.766224343846</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1755.85167388015</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>17558516738.8015</PartialPressure>
+ <PartialVolume>-0.0378938431055415</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid1</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid1</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>4</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1755.85167388015</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>17558516738.8015</PartialPressure>
+ <PartialVolume>-0.0378938431055415</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid2</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid2</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938431055415</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid3</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid3</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>6</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938431055415</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Aqueous</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Aqueous</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>7</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938431055415</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Solid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Solid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Compressor</Type>
+ <ObjectClass>PressureChangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OutletTemperature>389.231777541323</OutletTemperature>
+ <CalcMode>OutletPressure</CalcMode>
+ <ProcessPath>Adiabatic</ProcessPath>
+ <IgnorePhase>false</IgnorePhase>
+ <PolytropicEfficiency>99.9999999680797</PolytropicEfficiency>
+ <AdiabaticEfficiency>100</AdiabaticEfficiency>
+ <DeltaP>7500000</DeltaP>
+ <DeltaT>109.23177737426</DeltaT>
+ <DeltaQ>0.06314134144691</DeltaQ>
+ <POut>10000000</POut>
+ <AdiabaticCoefficient>1.31164972751309</AdiabaticCoefficient>
+ <PolytropicCoefficient>1.31164972676197</PolytropicCoefficient>
+ <AdiabaticHead>24311.5754104028</AdiabaticHead>
+ <PolytropicHead>24311.5754026425</PolytropicHead>
+ <EquipType></EquipType>
+ <CurvesDB></CurvesDB>
+ <CurveFlow>0</CurveFlow>
+ <CurveEff>0</CurveEff>
+ <CurveHead>0</CurveHead>
+ <CurvePower>0</CurvePower>
+ <Speed>1500</Speed>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>CompressorAdiabtico</ComponentDescription>
+ <ComponentName>COMP-28c24c39-5e16-4e03-a45a-5254d619ae04</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:31:18</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>COMP-28c24c39-5e16-4e03-a45a-5254d619ae04</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ <Curves>
+ <CurveSet RotationSpeed="1500">
+ <HEAD>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>HEAD</Name>
+ <ID>1342031c-af01-4ccb-a4fe-8f6d41fd2001</ID>
+ <CvType>Head</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
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+ </HEAD>
+ <EFF>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>EFF</Name>
+ <ID>e3fb35ca-d501-4e74-9295-b6d8742d5a75</ID>
+ <CvType>Efficiency</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
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+ </EFF>
+ <POWER>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>POWER</Name>
+ <ID>b7eecca3-db27-4023-b84a-1b0950249619</ID>
+ <CvType>Power</CvType>
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+ <x></x>
+ </POWER>
+ </CurveSet>
+ </Curves>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-b2d6055e-3a91-4329-9395-483685205892</ComponentName>
+ <EnergyFlow>0.0838060085271191</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-b2d6055e-3a91-4329-9395-483685205892</Name2>
+ <code>0</code>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:31:18</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
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+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-b2d6055e-3a91-4329-9395-483685205892</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-9ddb345f-d727-4135-b3c2-986245ab7350</ComponentName>
+ <Name2>MAT-9ddb345f-d727-4135-b3c2-986245ab7350</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ComponentName>Methane</ComponentName>
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+ <lnKvalue>0</lnKvalue>
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+ <MolarFlow>NaN</MolarFlow>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0</compressibilityFactor>
+ <density>NaN</density>
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+ <entropy>0</entropy>
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+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>NaN</kinematic_viscosity>
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+ <massfraction>0</massfraction>
+ <molar_enthalpy>NaN</molar_enthalpy>
+ <molar_entropy>NaN</molar_entropy>
+ <molarflow>0</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>NaN</molecularWeight>
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+ <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <MolarFlow>0.0173151610026005</MolarFlow>
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+ <DiffusionCoefficient>-Infinity</DiffusionCoefficient>
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+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
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+ <molarflow>0.0173151610026005</molarflow>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
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+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <gibbs_free_energy>0</gibbs_free_energy>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
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+ <Phase>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <ID>5</ID>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
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+ <Name>Methane</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid3</ComponentName>
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+ <Name>Liquid3</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <Phase>
+ <ID>6</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
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+ <MolarFlow>0</MolarFlow>
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+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Aqueous</ComponentName>
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+ <Properties>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <ComponentName>Solid</ComponentName>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
+ <ObjectClass>Exchangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
+ <OutletTemperature>280</OutletTemperature>
+ <OutletVaporFraction>1</OutletVaporFraction>
+ <CalcMode>OutletTemperature</CalcMode>
+ <Eficiencia>100</Eficiencia>
+ <DeltaT>-122.308657809878</DeltaT>
+ <DeltaQ>0.0838060085271191</DeltaQ>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>Resfriador</ComponentDescription>
+ <ComponentName>RESF-493907dc-edff-497e-b00d-d4d0e4549ca8</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
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+ <Calculated>true</Calculated>
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+ <Property>
+ <Name>Flow Conductance</Name>
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+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.Double</PropertyType>
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+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.Double</PropertyType>
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+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.Double</PropertyType>
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+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Double</PropertyType>
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+ </DynamicProperties>
+ <DynamicPropertiesDescriptions>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
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+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.String</PropertyType>
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+ <Property>
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+ <Property>
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+ <PropertyType>System.String</PropertyType>
+ <Data>"Empties the volume content on the next run."</Data>
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+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
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+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
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+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <AtEquilibrium>true</AtEquilibrium>
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+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
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+ <lnKvalue>NaN</lnKvalue>
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+ <MolarFlow>0.0173151610026005</MolarFlow>
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+ <VolumetricFraction>0.919770616379003</VolumetricFraction>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Mixture</ComponentName>
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+ <heatCapacityCv>2.01187093441481</heatCapacityCv>
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+ <molarflow>0.0173151610026005</molarflow>
+ <molecularWeight>16.04246</molecularWeight>
+ <pressure>2500000</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>402.308657809878</temperature>
+ <thermalConductivity>0.0498288780851708</thermalConductivity>
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+ <molar_helmholtz_energy>6786.35340303402</molar_helmholtz_energy>
+ <molar_internal_energy>461.010526624918</molar_internal_energy>
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+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <Name>Methane</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
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+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>NaN</kinematic_viscosity>
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+ <massfraction>0</massfraction>
+ <molar_enthalpy>NaN</molar_enthalpy>
+ <molar_entropy>NaN</molar_entropy>
+ <molarflow>0</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>NaN</molecularWeight>
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+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <molarflow>0.0173151610026005</molarflow>
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+ <molar_gibbs_free_energy>10077.3469582689</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>6786.35340303403</molar_helmholtz_energy>
+ <molar_internal_energy>461.010526624918</molar_internal_energy>
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+ <Compounds>
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+ <ComponentName>Methane</ComponentName>
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+ <Kvalue>0</Kvalue>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
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+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
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+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <Compounds>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Methane</ComponentName>
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+ <Molarity>0</Molarity>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
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+ <PartialVolume>-0.0378938445392739</PartialVolume>
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+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <gibbs_free_energy>0</gibbs_free_energy>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <ComponentName>Methane</ComponentName>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ComponentName>Aqueous</ComponentName>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Methane</ComponentName>
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+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
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+ <AdiabaticEfficiency>100</AdiabaticEfficiency>
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+ <CurvesDB></CurvesDB>
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+ <CurveHead>0</CurveHead>
+ <CurvePower>0</CurvePower>
+ <Speed>1500</Speed>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>CompressorAdiabtico</ComponentDescription>
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+ <Calculated>true</Calculated>
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+ <IsAdjustAttached>false</IsAdjustAttached>
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+ <Name>COMP-ac628f8f-34fb-45f0-9d15-dfd2f6ecdb44</Name>
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+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ <Curves>
+ <CurveSet RotationSpeed="1500">
+ <HEAD>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>HEAD</Name>
+ <ID>ed928fe8-e290-4cb1-a6ad-fe9ff59c0255</ID>
+ <CvType>Head</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
+ <y></y>
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+ </HEAD>
+ <EFF>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>EFF</Name>
+ <ID>dc10fa71-ad35-4d3d-bd74-de2ebaf99020</ID>
+ <CvType>Efficiency</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
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+ </EFF>
+ <POWER>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>POWER</Name>
+ <ID>cb0e306b-c066-4fa1-bdec-59e2913cee11</ID>
+ <CvType>Power</CvType>
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+ </POWER>
+ </CurveSet>
+ </Curves>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-94e99345-503b-42b9-acd8-39153040f7e4</ComponentName>
+ <EnergyFlow>0.0793532333016852</EnergyFlow>
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+ <Name2>EN-94e99345-503b-42b9-acd8-39153040f7e4</Name2>
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+ <DynamicsOnly>false</DynamicsOnly>
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+ <Calculated>true</Calculated>
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+ <SpecVarType>Source</SpecVarType>
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+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-1a4fefa7-343c-45d3-a3c3-04fa4f59b6d3</ComponentName>
+ <Name2>MAT-1a4fefa7-343c-45d3-a3c3-04fa4f59b6d3</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
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+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:30:10</LastUpdated>
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+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
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+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-1a4fefa7-343c-45d3-a3c3-04fa4f59b6d3</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ <Phases>
+ <Phase>
+ <ID>0</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>214.784013195057</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>8.0616619202825E-05</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Mixture</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Mixture</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>3.44566394032118</density>
+ <enthalpy>-45.5677697499365</enthalpy>
+ <entropy>-0.980063336659423</entropy>
+ <heatCapacityCp>2.22928794795568</heatCapacityCp>
+ <heatCapacityCv>1.6706709421551</heatCapacityCv>
+ <massflow>0.000277777777777778</massflow>
+ <molar_enthalpy>-731.019123502566</molar_enthalpy>
+ <molar_entropy>-15.7226268758253</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molecularWeight>16.04246</molecularWeight>
+ <pressure>500000</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>280.000000001659</temperature>
+ <thermalConductivity>0.0316935658937233</thermalConductivity>
+ <volumetric_flow>8.0616619202825E-05</volumetric_flow>
+ <gibbs_free_energy>228.849964516328</gibbs_free_energy>
+ <helmholtz_energy>85.7031080860658</helmholtz_energy>
+ <internal_energy>-188.714626180199</internal_energy>
+ <molar_gibbs_free_energy>3671.31640175461</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>1374.88868334639</molar_helmholtz_energy>
+ <molar_internal_energy>-3027.44684191079</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938415791843</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>OverallLiquid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0</compressibilityFactor>
+ <density>NaN</density>
+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>NaN</kinematic_viscosity>
+ <massflow>0</massflow>
+ <massfraction>0</massfraction>
+ <molar_enthalpy>NaN</molar_enthalpy>
+ <molar_entropy>NaN</molar_entropy>
+ <molarflow>0</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>NaN</molecularWeight>
+ <thermalConductivity>0</thermalConductivity>
+ <viscosity>0</viscosity>
+ <volumetric_flow>0</volumetric_flow>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0.011897511021527</ActivityCoeff>
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+ <MoleFraction>1</MoleFraction>
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+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>500000</PartialPressure>
+ <PartialVolume>4.65584000002759</PartialVolume>
+ <VolumetricFlow>8.0616619202825E-05</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>-Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
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+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.986471922744174</compressibilityFactor>
+ <density>3.44566394032118</density>
+ <enthalpy>-45.5677697499365</enthalpy>
+ <entropy>-0.980063336659424</entropy>
+ <heatCapacityCp>2.22928794795568</heatCapacityCp>
+ <heatCapacityCv>1.6706709421551</heatCapacityCv>
+ <jouleThomsonCoefficient>-4.02823197207409E-08</jouleThomsonCoefficient>
+ <kinematic_viscosity>3.13828663383981E-06</kinematic_viscosity>
+ <massflow>0.000277777777777778</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>-731.019123502566</molar_enthalpy>
+ <molar_entropy>-15.7226268758253</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>16.04246</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.0316935658937233</thermalConductivity>
+ <viscosity>1.08134810886138E-05</viscosity>
+ <volumetric_flow>8.0616619202825E-05</volumetric_flow>
+ <bulk_modulus>-35707.3509188701</bulk_modulus>
+ <gibbs_free_energy>228.849964516328</gibbs_free_energy>
+ <helmholtz_energy>85.7031080860658</helmholtz_energy>
+ <internal_energy>-188.714626180199</internal_energy>
+ <isothermal_compressibility>-2.8005437935513E-05</isothermal_compressibility>
+ <molar_gibbs_free_energy>3671.31640175461</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>1374.88868334639</molar_helmholtz_energy>
+ <molar_internal_energy>-3027.44684191079</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>5229.84839901164</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>2614924199.50582</PartialPressure>
+ <PartialVolume>-0.0378938415791843</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid1</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid1</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>4</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>5229.84839901164</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>2614924199.50582</PartialPressure>
+ <PartialVolume>-0.0378938415791843</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid2</ComponentName>
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+ <Name>Liquid2</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938415791843</PartialVolume>
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+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid3</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid3</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>6</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938415791843</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Aqueous</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Aqueous</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>7</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938415791843</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Solid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Solid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
+ <ObjectClass>Exchangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
+ <OutletTemperature>280</OutletTemperature>
+ <OutletVaporFraction>1</OutletVaporFraction>
+ <CalcMode>OutletTemperature</CalcMode>
+ <Eficiencia>100</Eficiencia>
+ <DeltaT>-120.580342373476</DeltaT>
+ <DeltaQ>0.0793532333016852</DeltaQ>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>Resfriador</ComponentDescription>
+ <ComponentName>RESF-4437c986-5958-4780-8cd8-c3549f6e1576</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:30:10</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>RESF-4437c986-5958-4780-8cd8-c3549f6e1576</Name>
+ <DynamicProperties>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>1.0</Data>
+ </Property>
+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>1.0</Data>
+ </Property>
+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>101325.0</Data>
+ </Property>
+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>1.0</Data>
+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>0.0</Data>
+ </Property>
+ </DynamicProperties>
+ <DynamicPropertiesDescriptions>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
+ </Property>
+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Cooler Volume"</Data>
+ </Property>
+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
+ </Property>
+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Empties the volume content on the next run."</Data>
+ </Property>
+ </DynamicPropertiesDescriptions>
+ <DynamicPropertiesUnitTypes>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>67</Data>
+ </Property>
+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>63</Data>
+ </Property>
+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>46</Data>
+ </Property>
+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>66</Data>
+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>66</Data>
+ </Property>
+ </DynamicPropertiesUnitTypes>
+ <AttachedUtilities />
+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-5ecd050b-1c61-43c7-bca4-c4635e3c907b</ComponentName>
+ <EnergyFlow>0.0781551539076061</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-5ecd050b-1c61-43c7-bca4-c4635e3c907b</Name2>
+ <code>0</code>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:18:17</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-5ecd050b-1c61-43c7-bca4-c4635e3c907b</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-a1358b61-5abc-42a4-9471-1a07a6cc735e</ComponentName>
+ <Name2>MAT-a1358b61-5abc-42a4-9471-1a07a6cc735e</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:30:10</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-a1358b61-5abc-42a4-9471-1a07a6cc735e</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ <Phases>
+ <Phase>
+ <ID>0</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>150.1309907986</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.000115333689003816</VolumetricFlow>
+ <VolumetricFraction>0.0623345796093615</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Mixture</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Mixture</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>2.40847041464691</density>
+ <enthalpy>240.103870132428</enthalpy>
+ <entropy>-0.13494887311377</entropy>
+ <heatCapacityCp>2.5414593789547</heatCapacityCp>
+ <heatCapacityCv>2.00747538571915</heatCapacityCv>
+ <massflow>0.000277777777777778</massflow>
+ <molar_enthalpy>3851.85673244468</molar_enthalpy>
+ <molar_entropy>-2.16491189897274</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molecularWeight>16.04246</molecularWeight>
+ <pressure>500000</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>400.580342373476</temperature>
+ <thermalConductivity>0.0495539786071748</thermalConductivity>
+ <volumetric_flow>0.000115333689003816</volumetric_flow>
+ <gibbs_free_energy>294.161735927257</gibbs_free_energy>
+ <helmholtz_energy>87.2974067150399</helmholtz_energy>
+ <internal_energy>33.2395409202109</internal_energy>
+ <molar_gibbs_free_energy>4719.07788214359</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>1400.46515532976</molar_helmholtz_energy>
+ <molar_internal_energy>533.244005630847</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.037893844033527</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>OverallLiquid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0</compressibilityFactor>
+ <density>NaN</density>
+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>NaN</kinematic_viscosity>
+ <massflow>0</massflow>
+ <massfraction>0</massfraction>
+ <molar_enthalpy>NaN</molar_enthalpy>
+ <molar_entropy>NaN</molar_entropy>
+ <molarflow>0</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>NaN</molecularWeight>
+ <thermalConductivity>0</thermalConductivity>
+ <viscosity>0</viscosity>
+ <volumetric_flow>0</volumetric_flow>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0.000732687601157065</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>150.1309907986</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>500000</PartialPressure>
+ <PartialVolume>6.66084993298616</PartialVolume>
+ <VolumetricFlow>0.000115333689003816</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>-Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.996453233506808</compressibilityFactor>
+ <density>2.40847041464691</density>
+ <enthalpy>240.103870132429</enthalpy>
+ <entropy>-0.13494887311377</entropy>
+ <heatCapacityCp>2.5414593789547</heatCapacityCp>
+ <heatCapacityCv>2.00747538571915</heatCapacityCv>
+ <jouleThomsonCoefficient>-7.38260988618018E-10</jouleThomsonCoefficient>
+ <kinematic_viscosity>5.99720093409481E-06</kinematic_viscosity>
+ <massflow>0.000277777777777778</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>3851.85673244468</molar_enthalpy>
+ <molar_entropy>-2.16491189897274</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>16.04246</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.0495539786071748</thermalConductivity>
+ <viscosity>1.44440810204601E-05</viscosity>
+ <volumetric_flow>0.000115333689003816</volumetric_flow>
+ <bulk_modulus>-93090.9854896304</bulk_modulus>
+ <gibbs_free_energy>294.161735927257</gibbs_free_energy>
+ <helmholtz_energy>87.2974067150399</helmholtz_energy>
+ <internal_energy>33.2395409202109</internal_energy>
+ <isothermal_compressibility>-1.07421786840079E-05</isothermal_compressibility>
+ <molar_gibbs_free_energy>4719.07788214359</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>1400.46515532976</molar_helmholtz_energy>
+ <molar_internal_energy>533.244005630847</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>40325.2634850773</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>20162631742.5387</PartialPressure>
+ <PartialVolume>-0.037893844033527</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid1</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid1</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>4</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>40325.2634850773</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>20162631742.5387</PartialPressure>
+ <PartialVolume>-0.037893844033527</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid2</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid2</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.037893844033527</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid3</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid3</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>6</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.037893844033527</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Aqueous</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Aqueous</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>7</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.037893844033527</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Solid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Solid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Compressor</Type>
+ <ObjectClass>PressureChangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OutletTemperature>400.580342373476</OutletTemperature>
+ <CalcMode>OutletPressure</CalcMode>
+ <ProcessPath>Adiabatic</ProcessPath>
+ <IgnorePhase>false</IgnorePhase>
+ <PolytropicEfficiency>99.999999999953</PolytropicEfficiency>
+ <AdiabaticEfficiency>100</AdiabaticEfficiency>
+ <DeltaP>400000</DeltaP>
+ <DeltaT>120.580342373476</DeltaT>
+ <DeltaQ>0.0781551539076061</DeltaQ>
+ <POut>500000</POut>
+ <AdiabaticCoefficient>1.28619913758745</AdiabaticCoefficient>
+ <PolytropicCoefficient>1.28619913758654</PolytropicCoefficient>
+ <AdiabaticHead>28656.9116883326</AdiabaticHead>
+ <PolytropicHead>28656.9116883192</PolytropicHead>
+ <EquipType></EquipType>
+ <CurvesDB></CurvesDB>
+ <CurveFlow>0</CurveFlow>
+ <CurveEff>0</CurveEff>
+ <CurveHead>0</CurveHead>
+ <CurvePower>0</CurvePower>
+ <Speed>1500</Speed>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>CompressorAdiabtico</ComponentDescription>
+ <ComponentName>COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:30:10</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ <Curves>
+ <CurveSet RotationSpeed="1500">
+ <HEAD>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>HEAD</Name>
+ <ID>3e273580-de52-4048-bdf4-d6be8116782b</ID>
+ <CvType>Head</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
+ <y></y>
+ <x></x>
+ </HEAD>
+ <EFF>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>EFF</Name>
+ <ID>da74c9c0-8a2b-477a-aa77-ae7263a3ed25</ID>
+ <CvType>Efficiency</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
+ <y></y>
+ <x></x>
+ </EFF>
+ <POWER>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>POWER</Name>
+ <ID>43edcce7-8d4a-4056-8f9e-6ec621dec3cc</ID>
+ <CvType>Power</CvType>
+ <yunit></yunit>
+ <xunit></xunit>
+ <y></y>
+ <x></x>
+ </POWER>
+ </CurveSet>
+ </Curves>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-8aae0cd5-5a00-4ced-86e6-1a47a4a675ac</ComponentName>
+ <Name2>MAT-8aae0cd5-5a00-4ced-86e6-1a47a4a675ac</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/16/2021 11:30:10</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-8aae0cd5-5a00-4ced-86e6-1a47a4a675ac</Name>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</PropertyPackage>
+ <Phases>
+ <Phase>
+ <ID>0</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>42.956802639266</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.000403083096011737</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Mixture</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Mixture</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>0.689132788068319</density>
+ <enthalpy>-41.2546839340519</enthalpy>
+ <entropy>-0.134949037350549</entropy>
+ <heatCapacityCp>2.20196493121492</heatCapacityCp>
+ <heatCapacityCv>1.6756812351885</heatCapacityCv>
+ <massflow>0.000277777777777778</massflow>
+ <molar_enthalpy>-661.826616824671</molar_enthalpy>
+ <molar_entropy>-2.16491453373469</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molecularWeight>16.04246</molecularWeight>
+ <pressure>100000</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>280</temperature>
+ <thermalConductivity>0.031693565893497</thermalConductivity>
+ <volumetric_flow>0.000403083096011737</volumetric_flow>
+ <gibbs_free_energy>-3.4689534758982</gibbs_free_energy>
+ <helmholtz_energy>-148.184539511604</helmholtz_energy>
+ <internal_energy>-185.970269969758</internal_energy>
+ <molar_gibbs_free_energy>-55.6505473789579</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-2377.24454773333</molar_helmholtz_energy>
+ <molar_internal_energy>-2983.42061717904</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938418374108</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>OverallLiquid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0</compressibilityFactor>
+ <density>NaN</density>
+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>NaN</kinematic_viscosity>
+ <massflow>0</massflow>
+ <massfraction>0</massfraction>
+ <molar_enthalpy>NaN</molar_enthalpy>
+ <molar_entropy>NaN</molar_entropy>
+ <molarflow>0</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>NaN</molecularWeight>
+ <thermalConductivity>0</thermalConductivity>
+ <viscosity>0</viscosity>
+ <volumetric_flow>0</volumetric_flow>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0.00237950220439316</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>42.956802639266</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.000277777777777778</MassFlow>
+ <MolarFlow>0.0173151610026005</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>100000</PartialPressure>
+ <PartialVolume>23.2792</PartialVolume>
+ <VolumetricFlow>0.000403083096011737</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>-Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.997282552817268</compressibilityFactor>
+ <density>0.689132788068318</density>
+ <enthalpy>-41.2546839340519</enthalpy>
+ <entropy>-0.134949037350549</entropy>
+ <heatCapacityCp>2.20196493121492</heatCapacityCp>
+ <heatCapacityCv>1.6756812351885</heatCapacityCv>
+ <jouleThomsonCoefficient>-4.0782161699461E-08</jouleThomsonCoefficient>
+ <kinematic_viscosity>1.56353902260384E-05</kinematic_viscosity>
+ <massflow>0.000277777777777778</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>-661.826616824671</molar_enthalpy>
+ <molar_entropy>-2.16491453373469</molar_entropy>
+ <molarflow>0.0173151610026005</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>16.04246</molecularWeight>
+ <speedOfSound>694.087653523697</speedOfSound>
+ <thermalConductivity>0.031693565893497</thermalConductivity>
+ <viscosity>1.0774860059006E-05</viscosity>
+ <volumetric_flow>0.000403083096011737</volumetric_flow>
+ <bulk_modulus>252646.077710577</bulk_modulus>
+ <gibbs_free_energy>-3.4689534758982</gibbs_free_energy>
+ <helmholtz_energy>-148.184539511604</helmholtz_energy>
+ <internal_energy>-185.970269969758</internal_energy>
+ <isothermal_compressibility>3.9581061739085E-06</isothermal_compressibility>
+ <molar_gibbs_free_energy>-55.6505473789579</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-2377.24454773333</molar_helmholtz_energy>
+ <molar_internal_energy>-2983.42061717905</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>26149.2419940069</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>2614924199.40069</PartialPressure>
+ <PartialVolume>-0.0378938418374108</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid1</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid1</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>4</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>26149.2419940069</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938418374108</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid2</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid2</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938418374108</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid3</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Liquid3</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>6</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938418374108</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Aqueous</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Aqueous</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>7</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Methane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Methane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0378938418374108</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Solid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Solid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>0</helmholtz_energy>
+ <internal_energy>0</internal_energy>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ </SimulationObjects>
+ <Settings>
+ <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables</Type>
+ <SelectedPropertyPackage>
+ <Type>DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage</Type>
+ <ComponentName>NRTL</ComponentName>
+ <ComponentDescription>In this Property Package, the NRTL (Non-Random Two-Liquid) model is used to calculate liquid-phase activity coefficients. Enthalpies are calculated by the Lee-Kesler model, while vapor-phase fugacities (optionally) and other thermodynamic properties (both phases) are calculated by the Peng-Robinson EOS.</ComponentDescription>
+ <Tag>NRTL (1)</Tag>
+ <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
+ <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
+ <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
+ <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
+ <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
+ <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
+ <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
+ <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
+ <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
+ <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
+ <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
+ <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
+ <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
+ <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
+ <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
+ <EnthalpyEntropyCpCvCalculationMode>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
+ <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
+ <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
+ <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
+ <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
+ <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
+ <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
+ <ForcedSolids>[]</ForcedSolids>
+ <PropertyOverrides>{}</PropertyOverrides>
+ <InteractionParameters_PR />
+ <InteractionParameters_NRTL />
+ <FlashSettings>
+ <Setting Name="Replace_PTFlash" Value="False" />
+ <Setting Name="ValidateEquilibriumCalc" Value="False" />
+ <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
+ <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
+ <Setting Name="ValidationGibbsTolerance" Value="0.01" />
+ <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+ <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+ <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+ <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+ <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="NL_FastMode" Value="True" />
+ <Setting Name="IO_FastMode" Value="True" />
+ <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
+ <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
+ <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
+ <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
+ <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
+ <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
+ <Setting Name="ST_Number_of_Random_Tries" Value="20" />
+ <Setting Name="CheckIncipientLiquidForStability" Value="False" />
+ <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
+ <Setting Name="PTFlash_DampingFactor" Value="1.0" />
+ <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
+ <Setting Name="ImmiscibleWaterOption" Value="False" />
+ <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
+ <Setting Name="UseIOFlash" Value="False" />
+ <Setting Name="GibbsMinimizationExternalSolver" Value="" />
+ <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
+ </FlashSettings>
+ </SelectedPropertyPackage>
+ <SimulationMode></SimulationMode>
+ <BackupFileName>17251524.dwbcs</BackupFileName>
+ <FilePath>F:\DWSIM\Flowsheet.dwxml</FilePath>
+ <FlowsheetQuickConnect>false</FlowsheetQuickConnect>
+ <FlowsheetShowCalculationQueue>false</FlowsheetShowCalculationQueue>
+ <FlowsheetShowConsoleWindow>false</FlowsheetShowConsoleWindow>
+ <FlowsheetShowCOReportsWindow>false</FlowsheetShowCOReportsWindow>
+ <FlowsheetShowWatchWindow>false</FlowsheetShowWatchWindow>
+ <FlowsheetMultiSelectMode>false</FlowsheetMultiSelectMode>
+ <FlowsheetSnapToGrid>false</FlowsheetSnapToGrid>
+ <FlowsheetDisplayGrid>false</FlowsheetDisplayGrid>
+ <FractionNumberFormat>G8</FractionNumberFormat>
+ <Key>DE7EC763C3B215940CCF51C1B01732DB3D29D4DC</Key>
+ <NumberFormat>G6</NumberFormat>
+ <Password></Password>
+ <SimulationAuthor>DESKTOP-B608FMG\preet_lk79p9y</SimulationAuthor>
+ <SimulationComments></SimulationComments>
+ <SimulationName>MySimulation_5</SimulationName>
+ <UsePassword>false</UsePassword>
+ <SelectedUnitSystem1>
+ <Type>DWSIM.SharedClasses.SystemsOfUnits.SIUnits_Custom5</Type>
+ <accel>m/s2</accel>
+ <activity>Pa</activity>
+ <activityCoefficient>-</activityCoefficient>
+ <area>m2</area>
+ <cakeresistance>m/kg</cakeresistance>
+ <cinematic_viscosity>m2/s</cinematic_viscosity>
+ <compressibility>1/Pa</compressibility>
+ <compressibilityFactor>-</compressibilityFactor>
+ <deltaP>bar</deltaP>
+ <deltaT>C.</deltaT>
+ <density>kg/m3</density>
+ <diameter>mm</diameter>
+ <distance>m</distance>
+ <enthalpy>kJ/kg</enthalpy>
+ <entropy>kJ/[kg.K]</entropy>
+ <excessEnthalpy>kJ/kg</excessEnthalpy>
+ <excessEntropy>kJ/[kg.K]</excessEntropy>
+ <force>N</force>
+ <foulingfactor>K.m2/W</foulingfactor>
+ <fugacity>Pa</fugacity>
+ <fugacityCoefficient>-</fugacityCoefficient>
+ <head>m</head>
+ <heat_transf_coeff>W/[m2.K]</heat_transf_coeff>
+ <heatCapacityCp>kJ/[kg.K]</heatCapacityCp>
+ <heatCapacityCv>kJ/[kg.K]</heatCapacityCv>
+ <heatflow>kW</heatflow>
+ <idealGasHeatCapacity>kJ/[kg.K]</idealGasHeatCapacity>
+ <jouleThomsonCoefficient>K/Pa</jouleThomsonCoefficient>
+ <kvalue>-</kvalue>
+ <logFugacityCoefficient>-</logFugacityCoefficient>
+ <logKvalue>-</logKvalue>
+ <mass>kg</mass>
+ <mass_conc>kg/m3</mass_conc>
+ <massflow>kg/h</massflow>
+ <massfraction>-</massfraction>
+ <mediumresistance>m-1</mediumresistance>
+ <molar_conc>kmol/m3</molar_conc>
+ <molar_enthalpy>kJ/kmol</molar_enthalpy>
+ <molar_entropy>kJ/[kmol.K]</molar_entropy>
+ <molar_volume>m3/kmol</molar_volume>
+ <molarflow>kmol/h</molarflow>
+ <molarfraction>-</molarfraction>
+ <molecularWeight>kg/kmol</molecularWeight>
+ <Name>C5</Name>
+ <pdp_boilingPointTemperature>C</pdp_boilingPointTemperature>
+ <pdp_meltingTemperature>C</pdp_meltingTemperature>
+ <pressure>bar</pressure>
+ <reac_rate>kmol/[m3.h]</reac_rate>
+ <reac_rate_heterog>kmol/[kg.s]</reac_rate_heterog>
+ <spec_vol>m3/kg</spec_vol>
+ <speedOfSound>m/s</speedOfSound>
+ <surfaceTension>N/m</surfaceTension>
+ <temperature>C</temperature>
+ <thermalConductivity>W/[m.K]</thermalConductivity>
+ <thermalConductivityOfLiquid>W/[m.K]</thermalConductivityOfLiquid>
+ <thermalConductivityOfVapor>W/[m.K]</thermalConductivityOfVapor>
+ <thickness>mm</thickness>
+ <time>h</time>
+ <vaporPressure>bar</vaporPressure>
+ <velocity>m/s</velocity>
+ <viscosity>Pa.s</viscosity>
+ <viscosityOfLiquid>Pa.s</viscosityOfLiquid>
+ <viscosityOfVapor>Pa.s</viscosityOfVapor>
+ <volume>m3</volume>
+ <volumetricFlow>m3/h</volumetricFlow>
+ <diffusivity>m2/s</diffusivity>
+ <conductance>[kg/s]/[Pa^0.5]</conductance>
+ </SelectedUnitSystem1>
+ <SimultaneousAdjustSolverEnabled>true</SimultaneousAdjustSolverEnabled>
+ <SpreadsheetUseRegionalSeparator>false</SpreadsheetUseRegionalSeparator>
+ <EnergyBalanceCheck>ShowWarning</EnergyBalanceCheck>
+ <MassBalanceCheck>ShowWarning</MassBalanceCheck>
+ <EnergyBalanceRelativeTolerance>0.01</EnergyBalanceRelativeTolerance>
+ <MassBalanceRelativeTolerance>0.01</MassBalanceRelativeTolerance>
+ <DisplayCornerPropertyList>false</DisplayCornerPropertyList>
+ <DisplayCornerPropertyListPosition>RightBottom</DisplayCornerPropertyListPosition>
+ <DisplayFloatingPropertyTables>true</DisplayFloatingPropertyTables>
+ <DisplayCornerPropertyListFontColor>DimGray</DisplayCornerPropertyListFontColor>
+ <DisplayCornerPropertyListFontName>Consolas</DisplayCornerPropertyListFontName>
+ <DisplayCornerPropertyListFontSize>8</DisplayCornerPropertyListFontSize>
+ <DisplayCornerPropertyListPadding>4</DisplayCornerPropertyListPadding>
+ <DefaultFloatingTableCompoundAmountBasis>Molar_Fractions</DefaultFloatingTableCompoundAmountBasis>
+ <DisplayFloatingTableCompoundAmounts>true</DisplayFloatingTableCompoundAmounts>
+ <SpreadsheetUnitLockingMode>true</SpreadsheetUnitLockingMode>
+ <CompoundOrderingMode>AsAdded</CompoundOrderingMode>
+ <FlowsheetControlPanelMode>false</FlowsheetControlPanelMode>
+ <SkipEquilibriumCalculationOnDefinedStreams>true</SkipEquilibriumCalculationOnDefinedStreams>
+ <ForceStreamPhase>None</ForceStreamPhase>
+ <DisplayUserDefinedPropertiesEditor>false</DisplayUserDefinedPropertiesEditor>
+ <VisibleProperties>
+ <ObjectType Value="AbsorptionColumn">
+ <PropertyID Value="PROP_AC_0" />
+ <PropertyID Value="PROP_AC_1" />
+ <PropertyID Value="PROP_AC_2" />
+ </ObjectType>
+ <ObjectType Value="Adjust">
+ <PropertyID Value="MinVal" />
+ <PropertyID Value="MaxVal" />
+ <PropertyID Value="AdjustValue" />
+ <PropertyID Value="Tolerance" />
+ <PropertyID Value="StepSize" />
+ <PropertyID Value="MaximumIterations" />
+ </ObjectType>
+ <ObjectType Value="AnalogGauge" />
+ <ObjectType Value="CapeOpenUO" />
+ <ObjectType Value="ComponentSeparator">
+ <PropertyID Value="PROP_CP_0" />
+ <PropertyID Value="SpecifiedStreamIndex" />
+ </ObjectType>
+ <ObjectType Value="Compressor">
+ <PropertyID Value="PROP_CO_0" />
+ <PropertyID Value="PROP_CO_1" />
+ <PropertyID Value="PROP_CO_2" />
+ <PropertyID Value="PROP_CO_3" />
+ <PropertyID Value="PROP_CO_4" />
+ <PropertyID Value="PolytropicEfficiency" />
+ <PropertyID Value="AdiabaticCoefficient" />
+ <PropertyID Value="PolytropicCoefficient" />
+ <PropertyID Value="AdiabaticHead" />
+ <PropertyID Value="PolytropicHead" />
+ <PropertyID Value="RotationSpeed" />
+ </ObjectType>
+ <ObjectType Value="Cooler">
+ <PropertyID Value="Flow Conductance" />
+ <PropertyID Value="Volume" />
+ <PropertyID Value="Minimum Pressure" />
+ <PropertyID Value="Initialize using Inlet Stream" />
+ <PropertyID Value="Reset Content" />
+ <PropertyID Value="PROP_CL_0" />
+ <PropertyID Value="PROP_CL_1" />
+ <PropertyID Value="PROP_CL_2" />
+ <PropertyID Value="PROP_CL_3" />
+ <PropertyID Value="PROP_CL_4" />
+ <PropertyID Value="PROP_CL_5" />
+ </ObjectType>
+ <ObjectType Value="CustomUO" />
+ <ObjectType Value="DigitalGauge" />
+ <ObjectType Value="DistillationColumn">
+ <PropertyID Value="PROP_DC_0" />
+ <PropertyID Value="PROP_DC_1" />
+ <PropertyID Value="PROP_DC_2" />
+ <PropertyID Value="PROP_DC_3" />
+ <PropertyID Value="PROP_DC_4" />
+ <PropertyID Value="PROP_DC_5" />
+ <PropertyID Value="PROP_DC_6" />
+ <PropertyID Value="PROP_DC_7" />
+ <PropertyID Value="Condenser_Specification_Value" />
+ <PropertyID Value="Reboiler_Specification_Value" />
+ <PropertyID Value="Global_Stage_Efficiency" />
+ <PropertyID Value="Condenser_Calculated_Value" />
+ <PropertyID Value="Reboiler_Calculated_Value" />
+ </ObjectType>
+ <ObjectType Value="DummyUnitOperation" />
+ <ObjectType Value="EnergyRecycle">
+ <PropertyID Value="PROP_ER_0" />
+ <PropertyID Value="PROP_ER_1" />
+ <PropertyID Value="PROP_ER_2" />
+ </ObjectType>
+ <ObjectType Value="EnergyStream">
+ <PropertyID Value="PROP_ES_0" />
+ </ObjectType>
+ <ObjectType Value="ExcelUO">
+ <PropertyID Value="Calc_dQ" />
+ </ObjectType>
+ <ObjectType Value="Expander">
+ <PropertyID Value="PROP_TU_0" />
+ <PropertyID Value="PROP_TU_1" />
+ <PropertyID Value="PROP_TU_2" />
+ <PropertyID Value="PROP_TU_3" />
+ <PropertyID Value="PROP_TU_4" />
+ <PropertyID Value="PolytropicEfficiency" />
+ <PropertyID Value="AdiabaticCoefficient" />
+ <PropertyID Value="PolytropicCoefficient" />
+ <PropertyID Value="AdiabaticHead" />
+ <PropertyID Value="PolytropicHead" />
+ <PropertyID Value="RotationSpeed" />
+ </ObjectType>
+ <ObjectType Value="Filter">
+ <PropertyID Value="PROP_FT_0" />
+ <PropertyID Value="PROP_FT_1" />
+ <PropertyID Value="PROP_FT_2" />
+ <PropertyID Value="PROP_FT_3" />
+ <PropertyID Value="PROP_FT_4" />
+ <PropertyID Value="PROP_FT_5" />
+ <PropertyID Value="PROP_FT_6" />
+ <PropertyID Value="PROP_FT_7" />
+ </ObjectType>
+ <ObjectType Value="Flowsheet" />
+ <ObjectType Value="Heater">
+ <PropertyID Value="Flow Conductance" />
+ <PropertyID Value="Volume" />
+ <PropertyID Value="Minimum Pressure" />
+ <PropertyID Value="Initialize using Inlet Stream" />
+ <PropertyID Value="Reset Content" />
+ <PropertyID Value="PROP_HT_0" />
+ <PropertyID Value="PROP_HT_1" />
+ <PropertyID Value="PROP_HT_2" />
+ <PropertyID Value="PROP_HT_3" />
+ <PropertyID Value="PROP_HT_4" />
+ <PropertyID Value="PROP_HT_5" />
+ </ObjectType>
+ <ObjectType Value="HeatExchanger">
+ <PropertyID Value="PROP_HX_0" />
+ <PropertyID Value="PROP_HX_1" />
+ <PropertyID Value="PROP_HX_2" />
+ <PropertyID Value="PROP_HX_3" />
+ <PropertyID Value="PROP_HX_4" />
+ <PropertyID Value="PROP_HX_25" />
+ <PropertyID Value="PROP_HX_26" />
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+ <PropertyID Value="PROP_HX_28" />
+ <PropertyID Value="PROP_HX_32" />
+ <PropertyID Value="PROP_HX_33" />
+ </ObjectType>
+ <ObjectType Value="Input" />
+ <ObjectType Value="LevelGauge" />
+ <ObjectType Value="MaterialStream">
+ <PropertyID Value="PROP_MS_0" />
+ <PropertyID Value="PROP_MS_1" />
+ <PropertyID Value="PROP_MS_2" />
+ <PropertyID Value="PROP_MS_3" />
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+ <ObjectType Value="Mixer" />
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+ <ObjectType Value="PIDController">
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+ <PropertyID Value="Kd" />
+ <PropertyID Value="Output" />
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+ <ObjectType Value="Pipe">
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+ <PropertyID Value="PROP_PS_2" />
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+ <PropertyID Value="PROP_PS_9" />
+ </ObjectType>
+ <ObjectType Value="Pump">
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+ <PropertyID Value="PROP_PU_2" />
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+ </ObjectType>
+ <ObjectType Value="Reactor_Conversion">
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+ </ObjectType>
+ <ObjectType Value="Reactor_CSTR">
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+ <PropertyID Value="Liquid Level" />
+ <PropertyID Value="Height" />
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+ <PropertyID Value="Calculation Mode" />
+ <PropertyID Value="Initial Gibbs Energy" />
+ <PropertyID Value="Final Gibbs Energy" />
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+ <PropertyID Value="PROP_GR_1" />
+ <PropertyID Value="Calculation Mode" />
+ <PropertyID Value="Initial Gibbs Energy" />
+ <PropertyID Value="Final Gibbs Energy" />
+ <PropertyID Value="Element Balance Residue" />
+ </ObjectType>
+ <ObjectType Value="Reactor_PFR">
+ <PropertyID Value="Max Sections" />
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+ <PropertyID Value="Calculation Mode" />
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+ <ObjectType Value="ReboiledAbsorber">
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+ <ObjectType Value="Recycle">
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+ </ObjectType>
+ <ObjectType Value="RefluxedAbsorber">
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+ <PropertyID Value="PROP_RF_3" />
+ <PropertyID Value="PROP_RF_4" />
+ <PropertyID Value="PROP_RF_5" />
+ <PropertyID Value="PROP_RF_6" />
+ </ObjectType>
+ <ObjectType Value="ShortcutColumn">
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+ <ObjectType Value="SolidsSeparator">
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+ </ObjectType>
+ <ObjectType Value="Splitter">
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+ <ObjectType Value="Switch" />
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+ <ObjectType Value="Valve">
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+ <ObjectType Value="Vessel">
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+ <PropertyID Value="PROP_SV_0" />
+ <PropertyID Value="PROP_SV_1" />
+ </ObjectType>
+ </VisibleProperties>
+ </Settings>
+ <DynamicProperties />
+ <GraphicObjects>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
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+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
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+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
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+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CompressorGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
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+ <LineColor>#ff4682b4</LineColor>
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+ <OverrideColors>false</OverrideColors>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Adiabatic Compressor</Description>
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+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Compressor</ObjectType>
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+ <Status>Calculated</Status>
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+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3</Name>
+ <Tag>COMP-01</Tag>
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+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-5ecd050b-1c61-43c7-bca4-c4635e3c907b" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
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+ </OutputConnectors>
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+ <Description>Material Stream</Description>
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+ <Description>Material Stream Cooler</Description>
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+ <ObjectType>Cooler</ObjectType>
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+ <Name>RESF-4437c986-5958-4780-8cd8-c3549f6e1576</Name>
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+ </InputConnectors>
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+ </OutputConnectors>
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+ <Description>Material Stream</Description>
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+ <ObjectType>MaterialStream</ObjectType>
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+ <Status>Calculated</Status>
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+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-1a4fefa7-343c-45d3-a3c3-04fa4f59b6d3</Name>
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+ </InputConnectors>
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+ </OutputConnectors>
+ <EnergyConnector>
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+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
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+ <IsEnergyStream>true</IsEnergyStream>
+ <ObjectType>EnergyStream</ObjectType>
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+ <Status>Calculated</Status>
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+ <IsConnector>false</IsConnector>
+ <Name>EN-94e99345-503b-42b9-acd8-39153040f7e4</Name>
+ <Tag>E-02</Tag>
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+ <Rotation>0</Rotation>
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+ </InputConnectors>
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+ <EnergyConnector>
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+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CompressorGraphic</Type>
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+ <LineWidth>1</LineWidth>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Adiabatic Compressor</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Compressor</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>COMP-ac628f8f-34fb-45f0-9d15-dfd2f6ecdb44</Name>
+ <Tag>COMP-02</Tag>
+ <Width>25</Width>
+ <X>615.5089</X>
+ <Y>29.50443</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-1a4fefa7-343c-45d3-a3c3-04fa4f59b6d3" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-1b9910bb-6249-4142-89af-5de0ecbaab93" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-0dc79c1f-4848-4acf-bc16-617e02926334" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
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+ <FillColor>#ffffffff</FillColor>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
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+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-0dc79c1f-4848-4acf-bc16-617e02926334</Name>
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+ <X>685.6517</X>
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+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="COMP-ac628f8f-34fb-45f0-9d15-dfd2f6ecdb44" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="RESF-493907dc-edff-497e-b00d-d4d0e4549ca8" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
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+ <ObjectType>EnergyStream</ObjectType>
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+ <Status>Calculated</Status>
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+ <Height>20</Height>
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+ <Rotation>0</Rotation>
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+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
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+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CoolerGraphic</Type>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
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+ <Description>Material Stream Cooler</Description>
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+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Cooler</ObjectType>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>RESF-493907dc-edff-497e-b00d-d4d0e4549ca8</Name>
+ <Tag>COOL-02</Tag>
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+ <Rotation>0</Rotation>
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+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-0dc79c1f-4848-4acf-bc16-617e02926334" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ </InputConnectors>
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+ </OutputConnectors>
+ <EnergyConnector AttachedFromObjID="RESF-493907dc-edff-497e-b00d-d4d0e4549ca8" AttachedFromConnIndex="-1" AttachedFromEnergyConn="False">
+ <Connector IsAttached="true" AttachedToObjID="EN-b2d6055e-3a91-4329-9395-483685205892" AttachedToConnIndex="0" AttachedToEnergyConn="True" />
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+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
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+ <LineWidth>1</LineWidth>
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+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
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+ <IsConnector>false</IsConnector>
+ <Name>MAT-9ddb345f-d727-4135-b3c2-986245ab7350</Name>
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+ </InputConnectors>
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+ </OutputConnectors>
+ <EnergyConnector>
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+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
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+ <ObjectType>EnergyStream</ObjectType>
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+ <Status>Calculated</Status>
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+ <Height>20</Height>
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+ <Name>EN-b2d6055e-3a91-4329-9395-483685205892</Name>
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+ <Rotation>90</Rotation>
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+ </InputConnectors>
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+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CompressorGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Adiabatic Compressor</Description>
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+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Compressor</ObjectType>
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+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>COMP-28c24c39-5e16-4e03-a45a-5254d619ae04</Name>
+ <Tag>COMP-03</Tag>
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+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
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+ </OutputConnectors>
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+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Name>MAT-486c6c7c-169a-4c8a-a2d7-891fc475656e</Name>
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+ </OutputConnectors>
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+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Name>EN-90ba5259-cb4d-47e2-97a1-0af0b609056d</Name>
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+ <Rotation>0</Rotation>
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+ </OutputConnectors>
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+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CoolerGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream Cooler</Description>
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+ <Shape>0</Shape>
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+ <AutoSize>false</AutoSize>
+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>RESF-b307edd3-c882-4180-b038-66e85210bd11</Name>
+ <Tag>COOL-03</Tag>
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+ <X>488.3054</X>
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+ <Rotation>0</Rotation>
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+ </InputConnectors>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
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+ <ObjectType>MaterialStream</ObjectType>
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+ <Name>MAT-35421d7f-ef01-477f-91ed-f27b109fa887</Name>
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+ </InputConnectors>
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+ </OutputConnectors>
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+ <LineWidth>1</LineWidth>
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+ <ObjectType>EnergyStream</ObjectType>
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+ <Name>EN-477f058c-274e-45a4-98a6-d2e3eca56a7e</Name>
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+ </InputConnectors>
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+ <EnergyConnector>
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+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.TurbineGraphic</Type>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <OverrideColors>false</OverrideColors>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Adiabatic Expander</Description>
+ <FlippedH>true</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Expander</ObjectType>
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+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
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+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>TURB-c985d75b-7bc8-4f75-8897-62bb6b8fede0</Name>
+ <Tag>EXP-01</Tag>
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+ <X>335.3888</X>
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+ <Selected>false</Selected>
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+ </InputConnectors>
+ <OutputConnectors>
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+ </OutputConnectors>
+ <EnergyConnector AttachedFromObjID="TURB-c985d75b-7bc8-4f75-8897-62bb6b8fede0" AttachedFromConnIndex="-1" AttachedFromEnergyConn="False">
+ <Connector IsAttached="true" AttachedToObjID="EN-95f446f4-bf77-4dce-b25f-8e94db426793" AttachedToConnIndex="0" AttachedToEnergyConn="True" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>true</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
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+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-5f834b55-1e31-45bb-88d6-23ce170be830</Name>
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+ <X>200.3312</X>
+ <Y>239.0314</Y>
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+ <Rotation>0</Rotation>
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+ </InputConnectors>
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+ </OutputConnectors>
+ <EnergyConnector>
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+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ </InputConnectors>
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+ <Calculated>true</Calculated>
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+ <Description>Vapor-Liquid Separator</Description>
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+ </InputConnectors>
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+ </OutputConnectors>
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+Molar Fraction (Vapor) 0 1 0.606341 0 1 1 1 1 1 1
+Molar Fraction (Mixture) / Methane 1 1 1 1 1 1 1 1 1 1
+Mass Fraction (Mixture) / Methane 1 1 1 1 1 1 1 1 1 1
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+ <SortBy>Name | DESC</SortBy>
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+ <PROP_MS_109_x002F_Methane>false</PROP_MS_109_x002F_Methane>
+ <PROP_MS_110_x002F_Methane>false</PROP_MS_110_x002F_Methane>
+ <PROP_MS_111_x002F_Methane>false</PROP_MS_111_x002F_Methane>
+ <PROP_MS_112_x002F_Methane>false</PROP_MS_112_x002F_Methane>
+ <PROP_MS_113_x002F_Methane>false</PROP_MS_113_x002F_Methane>
+ <PROP_MS_114_x002F_Methane>false</PROP_MS_114_x002F_Methane>
+ <PROP_MS_115_x002F_Methane>false</PROP_MS_115_x002F_Methane>
+ <PROP_MS_116_x002F_Methane>false</PROP_MS_116_x002F_Methane>
+ <PROP_MS_117_x002F_Methane>false</PROP_MS_117_x002F_Methane>
+ <PROP_MS_118_x002F_Methane>false</PROP_MS_118_x002F_Methane>
+ <PROP_MS_119_x002F_Methane>false</PROP_MS_119_x002F_Methane>
+ <PROP_MS_120_x002F_Methane>false</PROP_MS_120_x002F_Methane>
+ <PROP_MS_121_x002F_Methane>false</PROP_MS_121_x002F_Methane>
+ <PROP_MS_122_x002F_Methane>false</PROP_MS_122_x002F_Methane>
+ <PROP_MS_123_x002F_Methane>false</PROP_MS_123_x002F_Methane>
+ <PROP_MS_124_x002F_Methane>false</PROP_MS_124_x002F_Methane>
+ <PROP_MS_125_x002F_Methane>false</PROP_MS_125_x002F_Methane>
+ <PROP_MS_149_x002F_Methane>false</PROP_MS_149_x002F_Methane>
+ <PROP_MS_150_x002F_Methane>false</PROP_MS_150_x002F_Methane>
+ <PROP_MS_151_x002F_Methane>false</PROP_MS_151_x002F_Methane>
+ <PROP_MS_152_x002F_Methane>false</PROP_MS_152_x002F_Methane>
+ <PROP_MS_126>false</PROP_MS_126>
+ <PROP_MS_127>false</PROP_MS_127>
+ <PROP_MS_128>false</PROP_MS_128>
+ <PROP_MS_129>false</PROP_MS_129>
+ <PROP_MS_130>false</PROP_MS_130>
+ <PROP_MS_153>false</PROP_MS_153>
+ <PROP_MS_246>false</PROP_MS_246>
+ <PROP_MS_247>false</PROP_MS_247>
+ <PROP_MS_248>false</PROP_MS_248>
+ <PROP_MS_249>false</PROP_MS_249>
+ <PROP_MS_155>false</PROP_MS_155>
+ <PROP_MS_156>false</PROP_MS_156>
+ <PROP_MS_157>false</PROP_MS_157>
+ <PROP_MS_158>false</PROP_MS_158>
+ <PROP_MS_159>false</PROP_MS_159>
+ <PROP_MS_160>false</PROP_MS_160>
+ <PROP_MS_161>false</PROP_MS_161>
+ <PROP_MS_162>false</PROP_MS_162>
+ <PROP_MS_163>false</PROP_MS_163>
+ <PROP_MS_164>false</PROP_MS_164>
+ <PROP_MS_165>false</PROP_MS_165>
+ <PROP_MS_166>false</PROP_MS_166>
+ <PROP_MS_167>false</PROP_MS_167>
+ <PROP_MS_168>false</PROP_MS_168>
+ <PROP_MS_169>false</PROP_MS_169>
+ <PROP_MS_170>false</PROP_MS_170>
+ <PROP_MS_171>false</PROP_MS_171>
+ <PROP_MS_172>false</PROP_MS_172>
+ <PROP_MS_173>false</PROP_MS_173>
+ <PROP_MS_174>false</PROP_MS_174>
+ <PROP_MS_175>false</PROP_MS_175>
+ <PROP_MS_176>false</PROP_MS_176>
+ <PROP_MS_177>false</PROP_MS_177>
+ <PROP_MS_178>false</PROP_MS_178>
+ <PROP_MS_179>false</PROP_MS_179>
+ <PROP_MS_180>false</PROP_MS_180>
+ <PROP_MS_181>false</PROP_MS_181>
+ <PROP_MS_182>false</PROP_MS_182>
+ <PROP_MS_183>false</PROP_MS_183>
+ <PROP_MS_184>false</PROP_MS_184>
+ <PROP_MS_185>false</PROP_MS_185>
+ <PROP_MS_186>false</PROP_MS_186>
+ <PROP_MS_187>false</PROP_MS_187>
+ <PROP_MS_188>false</PROP_MS_188>
+ <PROP_MS_189>false</PROP_MS_189>
+ <PROP_MS_190>false</PROP_MS_190>
+ <PROP_MS_191>false</PROP_MS_191>
+ <PROP_MS_192>false</PROP_MS_192>
+ <PROP_MS_193>false</PROP_MS_193>
+ <PROP_MS_194>false</PROP_MS_194>
+ <PROP_MS_195>false</PROP_MS_195>
+ <PROP_MS_196>false</PROP_MS_196>
+ <PROP_MS_197>false</PROP_MS_197>
+ <PROP_MS_198>false</PROP_MS_198>
+ <PROP_MS_199>false</PROP_MS_199>
+ <PROP_MS_200>false</PROP_MS_200>
+ <PROP_MS_201>false</PROP_MS_201>
+ <PROP_MS_202>false</PROP_MS_202>
+ <PROP_MS_203>false</PROP_MS_203>
+ <PROP_MS_204>false</PROP_MS_204>
+ <PROP_MS_205>false</PROP_MS_205>
+ <PROP_MS_206>false</PROP_MS_206>
+ <PROP_MS_207>false</PROP_MS_207>
+ <PROP_MS_208>false</PROP_MS_208>
+ <PROP_MS_209>false</PROP_MS_209>
+ <PROP_MS_210>false</PROP_MS_210>
+ <PROP_MS_211>false</PROP_MS_211>
+ <PROP_MS_212>false</PROP_MS_212>
+ <PROP_MS_213>false</PROP_MS_213>
+ <PROP_MS_214>false</PROP_MS_214>
+ <PROP_MS_215>false</PROP_MS_215>
+ <PROP_MS_216>false</PROP_MS_216>
+ <PROP_MS_217>false</PROP_MS_217>
+ <PROP_MS_218>false</PROP_MS_218>
+ <PROP_MS_219>false</PROP_MS_219>
+ <PROP_MS_220>false</PROP_MS_220>
+ <PROP_MS_221>false</PROP_MS_221>
+ <PROP_MS_222>false</PROP_MS_222>
+ <PROP_MS_223>false</PROP_MS_223>
+ <PROP_MS_224>false</PROP_MS_224>
+ <PROP_MS_225>false</PROP_MS_225>
+ <PROP_MS_226>false</PROP_MS_226>
+ <PROP_MS_227>false</PROP_MS_227>
+ <PROP_MS_228>false</PROP_MS_228>
+ <PROP_MS_229>false</PROP_MS_229>
+ <PROP_MS_230>false</PROP_MS_230>
+ <PROP_MS_231>false</PROP_MS_231>
+ <PROP_MS_232_x002F_Methane>false</PROP_MS_232_x002F_Methane>
+ <PROP_MS_233_x002F_Methane>false</PROP_MS_233_x002F_Methane>
+ <PROP_MS_234_x002F_Methane>false</PROP_MS_234_x002F_Methane>
+ <PROP_MS_235_x002F_Methane>false</PROP_MS_235_x002F_Methane>
+ <PROP_MS_236_x002F_Methane>false</PROP_MS_236_x002F_Methane>
+ <PROP_MS_238_x002F_Methane>false</PROP_MS_238_x002F_Methane>
+ <PROP_MS_239_x002F_Methane>false</PROP_MS_239_x002F_Methane>
+ <PROP_MS_240_x002F_Methane>false</PROP_MS_240_x002F_Methane>
+ <PROP_MS_241_x002F_Methane>false</PROP_MS_241_x002F_Methane>
+ <PROP_MS_242_x002F_Methane>false</PROP_MS_242_x002F_Methane>
+ <PROP_MS_243_x002F_Methane>false</PROP_MS_243_x002F_Methane>
+ <PROP_MS_244_x002F_Methane>false</PROP_MS_244_x002F_Methane>
+ <PROP_MS_245_x002F_Methane>false</PROP_MS_245_x002F_Methane>
+ <PROP_MS_154>false</PROP_MS_154>
+ </Properties>
+ <SortableItems>
+ <SortableItem>Name | ASC</SortableItem>
+ <SortableItem>Name | DESC</SortableItem>
+ <SortableItem>Temperature | ASC</SortableItem>
+ <SortableItem>Temperature | DESC</SortableItem>
+ <SortableItem>Pressure | ASC</SortableItem>
+ <SortableItem>Pressure | DESC</SortableItem>
+ <SortableItem>Mass Flow | ASC</SortableItem>
+ <SortableItem>Mass Flow | DESC</SortableItem>
+ <SortableItem>Molar Flow | ASC</SortableItem>
+ <SortableItem>Molar Flow | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Methane | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Methane | DESC</SortableItem>
+ <SortableItem>Mass Fraction (Mixture) / Methane | ASC</SortableItem>
+ <SortableItem>Mass Fraction (Mixture) / Methane | DESC</SortableItem>
+ <SortableItem>Custom</SortableItem>
+ </SortableItems>
+ </GraphicObject>
+ </GraphicObjects>
+ <PropertyPackages>
+ <PropertyPackage>
+ <ID>PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d</ID>
+ <Type>DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage</Type>
+ <ComponentName>NRTL</ComponentName>
+ <ComponentDescription>In this Property Package, the NRTL (Non-Random Two-Liquid) model is used to calculate liquid-phase activity coefficients. Enthalpies are calculated by the Lee-Kesler model, while vapor-phase fugacities (optionally) and other thermodynamic properties (both phases) are calculated by the Peng-Robinson EOS.</ComponentDescription>
+ <Tag>NRTL (1)</Tag>
+ <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
+ <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
+ <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
+ <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
+ <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
+ <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
+ <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
+ <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
+ <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
+ <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
+ <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
+ <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
+ <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
+ <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
+ <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
+ <EnthalpyEntropyCpCvCalculationMode>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
+ <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
+ <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
+ <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
+ <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
+ <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
+ <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
+ <ForcedSolids>[]</ForcedSolids>
+ <PropertyOverrides>{}</PropertyOverrides>
+ <InteractionParameters_PR />
+ <InteractionParameters_NRTL />
+ <FlashSettings>
+ <Setting Name="Replace_PTFlash" Value="False" />
+ <Setting Name="ValidateEquilibriumCalc" Value="False" />
+ <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
+ <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
+ <Setting Name="ValidationGibbsTolerance" Value="0.01" />
+ <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+ <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+ <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+ <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+ <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
+ <Setting Name="NL_FastMode" Value="True" />
+ <Setting Name="IO_FastMode" Value="True" />
+ <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
+ <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
+ <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
+ <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
+ <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
+ <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
+ <Setting Name="ST_Number_of_Random_Tries" Value="20" />
+ <Setting Name="CheckIncipientLiquidForStability" Value="False" />
+ <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
+ <Setting Name="PTFlash_DampingFactor" Value="1.0" />
+ <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
+ <Setting Name="ImmiscibleWaterOption" Value="False" />
+ <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
+ <Setting Name="UseIOFlash" Value="False" />
+ <Setting Name="GibbsMinimizationExternalSolver" Value="" />
+ <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
+ </FlashSettings>
+ </PropertyPackage>
+ </PropertyPackages>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+ <Acentric_Factor>0.011</Acentric_Factor>
+ <BO_BSW>0</BO_BSW>
+ <BO_GOR>0</BO_GOR>
+ <BO_OilVisc1>0</BO_OilVisc1>
+ <BO_OilVisc2>0</BO_OilVisc2>
+ <BO_OilViscTemp1>0</BO_OilViscTemp1>
+ <BO_OilViscTemp2>0</BO_OilViscTemp2>
+ <BO_PNA_A>0</BO_PNA_A>
+ <BO_PNA_N>0</BO_PNA_N>
+ <BO_PNA_P>0</BO_PNA_P>
+ <BO_SGG>0</BO_SGG>
+ <BO_SGO>0</BO_SGO>
+ <CAS_Number>74-82-8</CAS_Number>
+ <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
+ <Chao_Seader_Liquid_Molar_Volume>37.8392</Chao_Seader_Liquid_Molar_Volume>
+ <Chao_Seader_Solubility_Parameter>0.00277501792024</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <Critical_Compressibility>0.286</Critical_Compressibility>
+ <Critical_Pressure>4599000</Critical_Pressure>
+ <Critical_Temperature>190.56</Critical_Temperature>
+ <Critical_Volume>0.0986</Critical_Volume>
+ <CurrentDB>ChemSep</CurrentDB>
+ <Dipole_Moment>0</Dipole_Moment>
+ <Electrolyte_Cp0>0</Electrolyte_Cp0>
+ <Electrolyte_DelGF>0</Electrolyte_DelGF>
+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
+ <EnthalpyOfFusionAtTf>0.9414</EnthalpyOfFusionAtTf>
+ <Formula>CH4</Formula>
+ <HVap_A>14418000</HVap_A>
+ <HVap_B>2.3055</HVap_B>
+ <HVap_C>-5.4199</HVap_C>
+ <HVap_D>5.658</HVap_D>
+ <HVap_E>-2.1286</HVap_E>
+ <HVap_TMAX>190.55</HVap_TMAX>
+ <HVap_TMIN>90.67</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>1</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>33151.9</Ideal_Gas_Heat_Capacity_Const_A>
+ <Ideal_Gas_Heat_Capacity_Const_B>-1220.001</Ideal_Gas_Heat_Capacity_Const_B>
+ <Ideal_Gas_Heat_Capacity_Const_C>12.0907</Ideal_Gas_Heat_Capacity_Const_C>
+ <Ideal_Gas_Heat_Capacity_Const_D>-0.000384791</Ideal_Gas_Heat_Capacity_Const_D>
+ <Ideal_Gas_Heat_Capacity_Const_E>9.896403E-08</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>16</IdealgasCpEquation>
+ <IG_Enthalpy_of_Formation_25C>-4645.17287248963</IG_Enthalpy_of_Formation_25C>
+ <IG_Entropy_of_Formation_25C>-5.02398104314258</IG_Entropy_of_Formation_25C>
+ <IG_Gibbs_Energy_of_Formation_25C>-3147.27292447667</IG_Gibbs_Energy_of_Formation_25C>
+ <InChI></InChI>
+ <Ion_CpAq_a>0</Ion_CpAq_a>
+ <Ion_CpAq_b>0</Ion_CpAq_b>
+ <Ion_CpAq_c>0</Ion_CpAq_c>
+ <IsBlackOil>false</IsBlackOil>
+ <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
+ <IsFPROPSSupported>false</IsFPROPSSupported>
+ <IsHydratedSalt>false</IsHydratedSalt>
+ <IsHYPO>0</IsHYPO>
+ <IsIon>false</IsIon>
+ <IsModified>false</IsModified>
+ <IsPF>0</IsPF>
+ <IsSalt>false</IsSalt>
+ <Liquid_Density_Const_A>1.894</Liquid_Density_Const_A>
+ <Liquid_Density_Const_B>0.23603</Liquid_Density_Const_B>
+ <Liquid_Density_Const_C>191.05</Liquid_Density_Const_C>
+ <Liquid_Density_Const_D>0.21974</Liquid_Density_Const_D>
+ <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+ <Liquid_Density_Tmax>191.04</Liquid_Density_Tmax>
+ <Liquid_Density_Tmin>90.68</Liquid_Density_Tmin>
+ <Liquid_Heat_Capacity_Const_A>61157</Liquid_Heat_Capacity_Const_A>
+ <Liquid_Heat_Capacity_Const_B>5034.1</Liquid_Heat_Capacity_Const_B>
+ <Liquid_Heat_Capacity_Const_C>-48.913</Liquid_Heat_Capacity_Const_C>
+ <Liquid_Heat_Capacity_Const_D>-0.22998</Liquid_Heat_Capacity_Const_D>
+ <Liquid_Heat_Capacity_Const_E>0.0022243</Liquid_Heat_Capacity_Const_E>
+ <Liquid_Heat_Capacity_Tmax>190</Liquid_Heat_Capacity_Tmax>
+ <Liquid_Heat_Capacity_Tmin>88.71</Liquid_Heat_Capacity_Tmin>
+ <Liquid_Thermal_Conductivity_Const_A>0.011567</Liquid_Thermal_Conductivity_Const_A>
+ <Liquid_Thermal_Conductivity_Const_B>-46.041</Liquid_Thermal_Conductivity_Const_B>
+ <Liquid_Thermal_Conductivity_Const_C>0.10435</Liquid_Thermal_Conductivity_Const_C>
+ <Liquid_Thermal_Conductivity_Const_D>-0.012133</Liquid_Thermal_Conductivity_Const_D>
+ <Liquid_Thermal_Conductivity_Const_E>-5.1716E-06</Liquid_Thermal_Conductivity_Const_E>
+ <Liquid_Thermal_Conductivity_Tmax>180</Liquid_Thermal_Conductivity_Tmax>
+ <Liquid_Thermal_Conductivity_Tmin>90.69</Liquid_Thermal_Conductivity_Tmin>
+ <Liquid_Viscosity_Const_A>-45.328</Liquid_Viscosity_Const_A>
+ <Liquid_Viscosity_Const_B>724.39</Liquid_Viscosity_Const_B>
+ <Liquid_Viscosity_Const_C>6.5917</Liquid_Viscosity_Const_C>
+ <Liquid_Viscosity_Const_D>-0.00010373</Liquid_Viscosity_Const_D>
+ <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+ <LiquidDensityEquation>105</LiquidDensityEquation>
+ <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
+ <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
+ <LiquidViscosityEquation>101</LiquidViscosityEquation>
+ <Molar_Weight>16.04246</Molar_Weight>
+ <MolarVolume_k1i>0</MolarVolume_k1i>
+ <MolarVolume_k2i>0</MolarVolume_k2i>
+ <MolarVolume_k3i>0</MolarVolume_k3i>
+ <MolarVolume_v2i>0</MolarVolume_v2i>
+ <MolarVolume_v3i>0</MolarVolume_v3i>
+ <Name>Methane</Name>
+ <NegativeIon></NegativeIon>
+ <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+ <Normal_Boiling_Point>111.66</Normal_Boiling_Point>
+ <OriginalDB>ChemSep</OriginalDB>
+ <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
+ <PC_SAFT_m>0</PC_SAFT_m>
+ <PC_SAFT_sigma>0</PC_SAFT_sigma>
+ <PositiveIon></PositiveIon>
+ <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
+ <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
+ <SMILES>C</SMILES>
+ <Solid_Density_Const_A>33.457</Solid_Density_Const_A>
+ <Solid_Density_Const_B>-0.033547</Solid_Density_Const_B>
+ <Solid_Density_Const_C>-0.000155</Solid_Density_Const_C>
+ <Solid_Density_Const_D>0</Solid_Density_Const_D>
+ <Solid_Density_Const_E>0</Solid_Density_Const_E>
+ <Solid_Density_Tmax>90.69</Solid_Density_Tmax>
+ <Solid_Density_Tmin>23.15</Solid_Density_Tmin>
+ <Solid_Heat_Capacity_Const_A>-3039.8</Solid_Heat_Capacity_Const_A>
+ <Solid_Heat_Capacity_Const_B>1292.4</Solid_Heat_Capacity_Const_B>
+ <Solid_Heat_Capacity_Const_C>-15.448</Solid_Heat_Capacity_Const_C>
+ <Solid_Heat_Capacity_Const_D>0.082442</Solid_Heat_Capacity_Const_D>
+ <Solid_Heat_Capacity_Const_E>-7.0636E-05</Solid_Heat_Capacity_Const_E>
+ <Solid_Heat_Capacity_Tmax>90.67</Solid_Heat_Capacity_Tmax>
+ <Solid_Heat_Capacity_Tmin>22.85</Solid_Heat_Capacity_Tmin>
+ <SolidDensityAtTs>0</SolidDensityAtTs>
+ <SolidDensityEquation>2</SolidDensityEquation>
+ <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
+ <SolidTs>0</SolidTs>
+ <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
+ <StandardStateMolarVolume>0</StandardStateMolarVolume>
+ <StoichSum>0</StoichSum>
+ <Surface_Tension_Const_A>-0.040703</Surface_Tension_Const_A>
+ <Surface_Tension_Const_B>-6.9523</Surface_Tension_Const_B>
+ <Surface_Tension_Const_C>-2.3114</Surface_Tension_Const_C>
+ <Surface_Tension_Const_D>-0.0055565</Surface_Tension_Const_D>
+ <Surface_Tension_Const_E>5.7595E-06</Surface_Tension_Const_E>
+ <Surface_Tension_Tmax>193.15</Surface_Tension_Tmax>
+ <Surface_Tension_Tmin>90</Surface_Tension_Tmin>
+ <SurfaceTensionEquation>16</SurfaceTensionEquation>
+ <TemperatureOfFusion>90.694</TemperatureOfFusion>
+ <UNIQUAC_Q>1.152</UNIQUAC_Q>
+ <UNIQUAC_R>1.1239</UNIQUAC_R>
+ <Vapor_Pressure_Constant_A>39.98844</Vapor_Pressure_Constant_A>
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