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-rw-r--r--Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Abstract.pdfbin0 -> 111131 bytes
-rw-r--r--Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Flowsheet.dwxml6020
-rw-r--r--Formic_Acid_Production_In_A_Reactive_Dividing_Wall_Column_By_Mr_Luis_Bayas_/user_defined_compound/1.json204
-rw-r--r--Kalina_Cycle_With_Double_Turbine_And_Reheating_By_Mr_Francis_Parra/Abstract.pdfbin0 -> 299631 bytes
-rw-r--r--Kalina_Cycle_With_Double_Turbine_And_Reheating_By_Mr_Francis_Parra/Flowsheet.dwxmzbin0 -> 86778 bytes
5 files changed, 6224 insertions, 0 deletions
diff --git a/Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Abstract.pdf b/Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Abstract.pdf
new file mode 100644
index 0000000..d386f3c
--- /dev/null
+++ b/Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Abstract.pdf
Binary files differ
diff --git a/Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Flowsheet.dwxml b/Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Flowsheet.dwxml
new file mode 100644
index 0000000..196b3b3
--- /dev/null
+++ b/Energy_Generation_Using_Co2_-_Closed_Loop_Thermodynamic_System_By_Mr_Naga_Mani_Deepak_Vusa/Flowsheet.dwxml
@@ -0,0 +1,6020 @@
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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>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
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+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
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+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
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+ <PartialVolume>0</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>Aqueous</ComponentName>
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+ <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>
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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>
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+ <ComponentName>Carbon dioxide</ComponentName>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.0770817973753928</MassFlow>
+ <MolarFlow>1.75148087061641</MolarFlow>
+ <Name>Carbon dioxide</Name>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <Name>HeavyWater</Name>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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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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+ <idealGasHeatCapacityCp>0.732808589957253</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.34733508373126</idealGasHeatCapacityRatio>
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+ </Phase>
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+ <MaximumIterations>10</MaximumIterations>
+ <MobileCompatible>true</MobileCompatible>
+ <ObjectClass>Logical</ObjectClass>
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+ <ProductName>Recycle Block</ProductName>
+ <ProductDescription>Block for connecting tear Material Streams</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
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+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <WegPars AccelDelay="2" AccelFreq="4" Qmax="0" Qmin="-20" />
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+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
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+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
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+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
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+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
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+ <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
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+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.018073516319719</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>
+ <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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0.294464524990441</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>766.494013113865</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>1</MassFlow>
+ <MolarFlow>22.7223667617219</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>1900000</PartialPressure>
+ <PartialVolume>0.0013046416317559</PartialVolume>
+ <VolumetricFlow>0.0296445456493688</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>6.75837001458993E-12</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>692.735913941236</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0013046416317559</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>
+ <compressibilityFactor>1</compressibilityFactor>
+ <density>33.7330182701347</density>
+ <enthalpy>3.39739994374092E-08</enthalpy>
+ <enthalpyF>-8941.47854437121</enthalpyF>
+ <entropy>-0.553758361212816</entropy>
+ <entropyF>-0.488216736476642</entropyF>
+ <heatCapacityCp>0.840137135566195</heatCapacityCp>
+ <heatCapacityCv>0.651223378309239</heatCapacityCv>
+ <jouleThomsonCoefficient>3.3139275116136E-09</jouleThomsonCoefficient>
+ <kinematic_viscosity>4.68812862135761E-07</kinematic_viscosity>
+ <massflow>1</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>1.49517872824066E-06</molar_enthalpy>
+ <molar_entropy>-24.3706285977954</molar_entropy>
+ <molarflow>22.7223667617219</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>44.0095</molecularWeight>
+ <speedOfSound>269.562390522599</speedOfSound>
+ <thermalConductivity>0.016560210624645</thermalConductivity>
+ <viscosity>1.58144728436998E-05</viscosity>
+ <volumetric_flow>0.0296445456493688</volumetric_flow>
+ <bulk_modulus>1900000</bulk_modulus>
+ <gibbs_free_energy>165.103055451968</gibbs_free_energy>
+ <helmholtz_energy>108.778418718168</helmholtz_energy>
+ <internal_energy>-56.3246366998268</internal_energy>
+ <isothermal_compressibility>5.26315789473684E-07</isothermal_compressibility>
+ <molar_gibbs_free_energy>7266.1029189134</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>4787.28381857719</molar_helmholtz_energy>
+ <molar_internal_energy>-2478.81909884103</molar_internal_energy>
+ <idealGasHeatCapacityCp>0.840137135566195</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.29009056423532</idealGasHeatCapacityRatio>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>3.39599481476577</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>6452390.14805495</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.00144355154666462</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>3.39599481476577</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>6452390.14805495</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.00144355154666462</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>298.15</OutletTemperature>
+ <OutletVaporFraction>1</OutletVaporFraction>
+ <CalcMode>OutletTemperature</CalcMode>
+ <Eficiencia>100</Eficiencia>
+ <DeltaT>81.57</DeltaT>
+ <DeltaQ>-575.680890801633</DeltaQ>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>Resfriador</ComponentDescription>
+ <ComponentName>RESF-99f50845-cd88-4de0-b865-53da15112ae4</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/29/2022 21:20:16</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>RESF-99f50845-cd88-4de0-b865-53da15112ae4</Name>
+ <ProductName>Cooler</ProductName>
+ <ProductDescription>Simple cooler model</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.0.4.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <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-4969b289-f9ab-48e5-b866-1c3761d97dbb</PropertyPackage>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-8595d51c-1021-4001-b107-6f2795383db7</ComponentName>
+ <EnergyFlow>-6.79503866898271E-08</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-8595d51c-1021-4001-b107-6f2795383db7</Name2>
+ <code>0</code>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/29/2022 21:20:16</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-8595d51c-1021-4001-b107-6f2795383db7</Name>
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.0.4.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Expander</Type>
+ <ObjectClass>PressureChangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <CalcMode>OutletPressure</CalcMode>
+ <OutletTemperature>194.152656752023</OutletTemperature>
+ <ProcessPath>Adiabatic</ProcessPath>
+ <IgnorePhase>false</IgnorePhase>
+ <PolytropicEfficiency>100</PolytropicEfficiency>
+ <AdiabaticEfficiency>100</AdiabaticEfficiency>
+ <DeltaP>1798675</DeltaP>
+ <DeltaT>-103.997343247974</DeltaT>
+ <DeltaQ>124.130700962427</DeltaQ>
+ <POut>101325</POut>
+ <AdiabaticCoefficient>1.17142143564289</AdiabaticCoefficient>
+ <PolytropicCoefficient>1.17142143564289</PolytropicCoefficient>
+ <AdiabaticHead>13699.5970609009</AdiabaticHead>
+ <PolytropicHead>13699.5970609009</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>TurbinaAdiabtica</ComponentDescription>
+ <ComponentName>TURB-988fd0e2-d166-496a-b5d1-6d8e6abb8cf9</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/29/2022 21:20:16</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>TURB-988fd0e2-d166-496a-b5d1-6d8e6abb8cf9</Name>
+ <ProductName>Expander (Turbine)</ProductName>
+ <ProductDescription>Adiabatic/Polytropic Turbine Expansion Model</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.0.4.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-4969b289-f9ab-48e5-b866-1c3761d97dbb</PropertyPackage>
+ <Curves>
+ <CurveSet RotationSpeed="1500">
+ <HEAD>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve</Type>
+ <Enabled>false</Enabled>
+ <Name>HEAD</Name>
+ <ID>5f20bbcb-8c93-4ee6-ad5c-2b948f498285</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>a3728b72-ec16-4447-a958-2f172416292a</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>76d61438-d52c-47a8-b47b-791d1dcd3165</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>
+ <TotalEnergyFlow>-8941.47854440518</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-c2a9ba92-a2b5-42c2-98e1-52084ed0fd75</ComponentName>
+ <Name2>MAT-c2a9ba92-a2b5-42c2-98e1-52084ed0fd75</Name2>
+ <code>0</code>
+ <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>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/29/2022 21:20:16</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-c2a9ba92-a2b5-42c2-98e1-52084ed0fd75</Name>
+ <ProductName>Material Stream</ProductName>
+ <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.0.4.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-4969b289-f9ab-48e5-b866-1c3761d97dbb</PropertyPackage>
+ <Phases>
+ <Phase>
+ <ID>0</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>766.494013217834</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>1</MassFlow>
+ <MolarFlow>22.7223667617219</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.0296445456453478</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>33.7330182747103</density>
+ <enthalpy>-2.3878133547592E-12</enthalpy>
+ <entropy>-0.553758361326773</entropy>
+ <heatCapacityCp>0.840137135525297</heatCapacityCp>
+ <heatCapacityCv>0.651223378268341</heatCapacityCv>
+ <massflow>1</massflow>
+ <massfraction>0</massfraction>
+ <molar_enthalpy>-1.05086471836275E-10</molar_enthalpy>
+ <molar_entropy>-24.3706286028106</molar_entropy>
+ <molarflow>22.7223667617219</molarflow>
+ <molarfraction>0</molarfraction>
+ <molecularWeight>44.0095</molecularWeight>
+ <pressure>1900000</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>298.149999999997</temperature>
+ <thermalConductivity>0.0165602106215303</thermalConductivity>
+ <volumetric_flow>0.0296445456453478</volumetric_flow>
+ <gibbs_free_energy>165.103055429574</gibbs_free_energy>
+ <helmholtz_energy>108.778418703413</helmholtz_energy>
+ <internal_energy>-56.3246367261632</internal_energy>
+ <molar_gibbs_free_energy>7266.10291792782</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>4787.28381792784</molar_helmholtz_energy>
+ <molar_internal_energy>-2478.81910000008</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0616781661670829</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0180735163196535</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>
+ <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>
+ <pressure>0</pressure>
+ <temperature>0</temperature>
+ <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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0.2944645252631</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>766.494013217834</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>1</MassFlow>
+ <MolarFlow>22.7223667617219</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>1900000</PartialPressure>
+ <PartialVolume>0.00130464163157893</PartialVolume>
+ <VolumetricFlow>0.0296445456453478</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>6.75837001298568E-12</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>692.735915661067</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.00130464163157893</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>
+ <compressibilityFactor>1</compressibilityFactor>
+ <density>33.7330182747103</density>
+ <enthalpy>-2.3878133547592E-12</enthalpy>
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+ <gibbs_free_energy>109.923913109073</gibbs_free_energy>
+ <helmholtz_energy>109.612832608341</helmholtz_energy>
+ <internal_energy>-575.991971302366</internal_energy>
+ <molar_gibbs_free_energy>4837.69645397376</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>4824.00595667678</molar_helmholtz_energy>
+ <molar_internal_energy>-25349.1186610315</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>26878.6079868573</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.193674478942442</MassFlow>
+ <MolarFlow>4.40074254291556</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0372749361368113</PartialVolume>
+ <VolumetricFlow>0.000163726579332805</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.568103019415949</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>0.0392571220391773</compressibilityFactor>
+ <density>1182.91409819759</density>
+ <enthalpy>-410.438161972219</enthalpy>
+ <entropy>-2.40263216862726</entropy>
+ <heatCapacityCp>1.85239473738251</heatCapacityCp>
+ <heatCapacityCv>1.85239473738251</heatCapacityCv>
+ <kinematic_viscosity>2.11697018451394E-07</kinematic_viscosity>
+ <massflow>0.193674478942442</massflow>
+ <massfraction>0.193674478942442</massfraction>
+ <molar_enthalpy>-18063.1782893164</molar_enthalpy>
+ <molar_entropy>-105.738640425201</molar_entropy>
+ <molarflow>4.40074254291556</molarflow>
+ <molarfraction>0.193674478942442</molarfraction>
+ <molecularWeight>44.0095</molecularWeight>
+ <thermalConductivity>0.178286839115038</thermalConductivity>
+ <viscosity>0.00025041938767255</viscosity>
+ <volumetric_flow>0.000163726579332805</volumetric_flow>
+ <gibbs_free_energy>109.923913109073</gibbs_free_energy>
+ <helmholtz_energy>108.317710255548</helmholtz_energy>
+ <internal_energy>-412.044364825744</internal_energy>
+ <molar_gibbs_free_energy>4837.69645397376</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>4767.00826949155</molar_helmholtz_energy>
+ <molar_internal_energy>-18133.8664737986</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>1900000</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>3.86289721683109E-12</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>
+ <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>
+ <idealGasHeatCapacityCp>0.884284807813163</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.27167331327045</idealGasHeatCapacityRatio>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</ComponentName>
+ <ActivityCoeff>1</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>26878.6079868573</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.272671955820242</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.193674478942442</MassFlow>
+ <MolarFlow>4.40074254291556</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>1900000</PartialPressure>
+ <PartialVolume>0.0372749361368113</PartialVolume>
+ <VolumetricFlow>0.000163726579332805</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>4.84289655169332E-09</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>1</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
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+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>8.81778807143905E-07</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.568103019415949</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>6.37293249514127E-10</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>
+ <compressibilityFactor>0.0392571220391773</compressibilityFactor>
+ <density>1182.91409819759</density>
+ <enthalpy>-410.438161972219</enthalpy>
+ <enthalpyF>-9351.9167063774</enthalpyF>
+ <entropy>-2.40263216862726</entropy>
+ <entropyF>-2.33709054389109</entropyF>
+ <heatCapacityCp>1.85239473738251</heatCapacityCp>
+ <heatCapacityCv>1.85239473738251</heatCapacityCv>
+ <jouleThomsonCoefficient>-2.14456448937664E-10</jouleThomsonCoefficient>
+ <kinematic_viscosity>2.11697018451394E-07</kinematic_viscosity>
+ <massflow>0.193674478942442</massflow>
+ <massfraction>0.193674478942442</massfraction>
+ <molar_enthalpy>-18063.1782893164</molar_enthalpy>
+ <molar_entropy>-105.738640425201</molar_entropy>
+ <molarflow>4.40074254291556</molarflow>
+ <molarfraction>0.193674478942442</molarfraction>
+ <molecularWeight>44.0095</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.178286839115038</thermalConductivity>
+ <viscosity>0.00025041938767255</viscosity>
+ <volumetric_flow>0.000163726579332805</volumetric_flow>
+ <bulk_modulus>-4.08613036493888</bulk_modulus>
+ <gibbs_free_energy>109.923913109073</gibbs_free_energy>
+ <helmholtz_energy>108.317710255548</helmholtz_energy>
+ <internal_energy>-412.044364825744</internal_energy>
+ <isothermal_compressibility>-0.244730322013345</isothermal_compressibility>
+ <molar_gibbs_free_energy>4837.69645397376</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>4767.00826949155</molar_helmholtz_energy>
+ <molar_internal_energy>-18133.8664737986</molar_internal_energy>
+ <idealGasHeatCapacityCp>0.75548985861277</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.33343050793157</idealGasHeatCapacityRatio>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>4</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>518076.716058459</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
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+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>8.81778807143905E-07</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
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+ <Molarity>0</Molarity>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
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+ <PartialVolume>0</PartialVolume>
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+ <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>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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>34585.09982</Molarity>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.806325521057558</MassFlow>
+ <MolarFlow>18.3216242188063</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
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+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
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+ <CompositionBasis>Molar_Fractions</CompositionBasis>
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+ <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
+ <molar_internal_energy>NaN</molar_internal_energy>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>101324.907280208</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>5.80643436651923E-07</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.999999084926802</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>101324.907280208</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>5.80643436651923E-07</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</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>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</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>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>35357.0714019386</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.0770817973753928</MassFlow>
+ <MolarFlow>1.75148087061641</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>HeavyWater</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>HeavyWater</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <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>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>
+ <compressibilityFactor>0</compressibilityFactor>
+ <density>1556.04703386362</density>
+ <enthalpy>-631.225937444434</enthalpy>
+ <enthalpyF>-9572.70448184961</enthalpyF>
+ <entropy>-3.16559610264432</entropy>
+ <entropyF>-3.10005447790814</entropyF>
+ <heatCapacityCp>1.268574350385</heatCapacityCp>
+ <heatCapacityCv>1.268574350385</heatCapacityCv>
+ <jouleThomsonCoefficient>0</jouleThomsonCoefficient>
+ <kinematic_viscosity>1E+20</kinematic_viscosity>
+ <massflow>0.0770817973753928</massflow>
+ <massfraction>0.0770817973753928</massfraction>
+ <molar_enthalpy>-27779.9378939608</molar_enthalpy>
+ <molar_entropy>-139.316301679325</molar_entropy>
+ <molarflow>1.75148087061641</molarflow>
+ <molarfraction>0.0770817973753928</molarfraction>
+ <molecularWeight>44.0095</molecularWeight>
+ <speedOfSound>0</speedOfSound>
+ <thermalConductivity>0</thermalConductivity>
+ <viscosity>1E+20</viscosity>
+ <volumetric_flow>4.95369328162279E-05</volumetric_flow>
+ <bulk_modulus>0</bulk_modulus>
+ <gibbs_free_energy>-16.6170439121901</gibbs_free_energy>
+ <helmholtz_energy>-16.6170439121901</helmholtz_energy>
+ <internal_energy>-631.225937444434</internal_energy>
+ <isothermal_compressibility>0</isothermal_compressibility>
+ <molar_gibbs_free_energy>-731.307794053529</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-731.307794053529</molar_helmholtz_energy>
+ <molar_internal_energy>-27779.9378939608</molar_internal_energy>
+ <idealGasHeatCapacityCp>0.732808589957253</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.34733508373126</idealGasHeatCapacityRatio>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-c4d90083-5d18-465c-b70a-1e138e037b07</ComponentName>
+ <EnergyFlow>124.130700962427</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-c4d90083-5d18-465c-b70a-1e138e037b07</Name2>
+ <code>0</code>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/29/2022 21:20:16</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-c4d90083-5d18-465c-b70a-1e138e037b07</Name>
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.0.4.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Heater</Type>
+ <ObjectClass>Exchangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
+ <FixOnHeat>true</FixOnHeat>
+ <Eficiencia>100</Eficiencia>
+ <OutletVaporFraction>1</OutletVaporFraction>
+ <OutletTemperature>298.149999999997</OutletTemperature>
+ <CalcMode>HeatAdded</CalcMode>
+ <DeltaT>-4.04414777221973E-08</DeltaT>
+ <DeltaQ>-6.79503866898271E-08</DeltaQ>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>Aquecedor</ComponentDescription>
+ <ComponentName>AQ-ab8e71d7-ef71-4e8d-b843-9576e01d324f</ComponentName>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>09/29/2022 21:20:16</LastUpdated>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>AQ-ab8e71d7-ef71-4e8d-b843-9576e01d324f</Name>
+ <ProductName>Heater</ProductName>
+ <ProductDescription>Simple heater model</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.0.4.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <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>"Heater 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-4969b289-f9ab-48e5-b866-1c3761d97dbb</PropertyPackage>
+ </SimulationObject>
+ </SimulationObjects>
+ <Settings>
+ <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables</Type>
+ <SelectedPropertyPackage>
+ <Type>DWSIM.Thermodynamics.PropertyPackages.RaoultPropertyPackage</Type>
+ <ComponentName>Raoult's Law</ComponentName>
+ <ComponentDescription>Reference Property Package (Ideal Gas/Solution).</ComponentDescription>
+ <Tag>Raoult's Law (1)</Tag>
+ <SingleCompoundCheckThreshold>0.99999</SingleCompoundCheckThreshold>
+ <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>
+ <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="" />
+ <Setting Name="PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases" Value="True" />
+ <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
+ </FlashSettings>
+ </SelectedPropertyPackage>
+ <SimulationMode></SimulationMode>
+ <BackupFileName>83040633.dwbcs</BackupFileName>
+ <FilePath>C:\Users\madti\Desktop\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>84465FED04C95F89EC8201B61AD334A93D103CC9</Key>
+ <NumberFormat>G6</NumberFormat>
+ <Password></Password>
+ <SimulationAuthor>LAPTOP-PO6B0HI3\madti</SimulationAuthor>
+ <SimulationComments></SimulationComments>
+ <SimulationName>MySimulation_34</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>
+ <gor>m3/m3</gor>
+ <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>
+ <LabelFontSize>10</LabelFontSize>
+ <FlowsheetColorTheme>0</FlowsheetColorTheme>
+ <RegularFontName>OpenSans_SemiCondensed-Regular</RegularFontName>
+ <BoldFontName>OpenSans_SemiCondensed-SemiBold</BoldFontName>
+ <ItalicFontName>OpenSans_SemiCondensed-Italic</ItalicFontName>
+ <BoldItalicFontName>OpenSans_SemiCondensed-MediumItalic</BoldItalicFontName>
+ <DisplayEnergyStreamPowerValue>true</DisplayEnergyStreamPowerValue>
+ <DisplayMaterialStreamMassFlowValue>false</DisplayMaterialStreamMassFlowValue>
+ <DisplayMaterialStreamMolarFlowValue>false</DisplayMaterialStreamMolarFlowValue>
+ <DisplayMaterialStreamVolFlowValue>false</DisplayMaterialStreamVolFlowValue>
+ <DisplayMaterialStreamTemperatureValue>false</DisplayMaterialStreamTemperatureValue>
+ <DisplayMaterialStreamPressureValue>false</DisplayMaterialStreamPressureValue>
+ <DisplayMaterialStreamEnergyFlowValue>false</DisplayMaterialStreamEnergyFlowValue>
+ <AddObjectsWithStreams>2</AddObjectsWithStreams>
+ <DisplayDynamicPropertyValues>true</DisplayDynamicPropertyValues>
+ <CurrentWeather>
+ <Type>DWSIM.SharedClasses.WeatherData</Type>
+ <CurrentCondition>Sunny</CurrentCondition>
+ <WindSpeed_km_h>5</WindSpeed_km_h>
+ <RelativeHumidity_pct>30</RelativeHumidity_pct>
+ <Temperature_C>30</Temperature_C>
+ <SolarIrradiation_kWh_m2>1</SolarIrradiation_kWh_m2>
+ <Latitude>0</Latitude>
+ <Longitude>0</Longitude>
+ <AtmosphericPressure_Pa>101325</AtmosphericPressure_Pa>
+ </CurrentWeather>
+ <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_5" />
+ <PropertyID Value="PROP_DC_6" />
+ <PropertyID Value="PROP_DC_7" />
+ <PropertyID Value="PROP_DC_8" />
+ <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" />
+ <PropertyID Value="PROP_HX_27" />
+ <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" />
+ <PropertyID Value="PROP_MS_4" />
+ <PropertyID Value="PROP_MS_9" />
+ <PropertyID Value="PROP_MS_10" />
+ <PropertyID Value="PROP_MS_27" />
+ <PropertyID Value="PROP_MS_130" />
+ <PropertyID Value="PROP_MS_154" />
+ </ObjectType>
+ <ObjectType Value="Mixer" />
+ <ObjectType Value="OrificePlate">
+ <PropertyID Value="PROP_OP_0" />
+ <PropertyID Value="PROP_OP_1" />
+ <PropertyID Value="PROP_OP_2" />
+ <PropertyID Value="PROP_OP_3" />
+ <PropertyID Value="PROP_OP_4" />
+ <PropertyID Value="PROP_OP_5" />
+ <PropertyID Value="PROP_OP_6" />
+ <PropertyID Value="PROP_OP_7" />
+ </ObjectType>
+ <ObjectType Value="PIDController">
+ <PropertyID Value="Active" />
+ <PropertyID Value="ManualOverride" />
+ <PropertyID Value="LastError" />
+ <PropertyID Value="CurrentError" />
+ <PropertyID Value="CumulativeError" />
+ <PropertyID Value="SetPoint" />
+ <PropertyID Value="SetPointAbs" />
+ <PropertyID Value="Kp" />
+ <PropertyID Value="Ki" />
+ <PropertyID Value="Kd" />
+ <PropertyID Value="Output" />
+ <PropertyID Value="OutputMin" />
+ <PropertyID Value="OutputMax" />
+ <PropertyID Value="OutputAbs" />
+ </ObjectType>
+ <ObjectType Value="Pipe">
+ <PropertyID Value="PROP_PS_0" />
+ <PropertyID Value="PressureDropStatic" />
+ <PropertyID Value="PressureDropFriction" />
+ <PropertyID Value="PROP_PS_1" />
+ <PropertyID Value="PROP_PS_2" />
+ <PropertyID Value="PROP_PS_8" />
+ <PropertyID Value="PROP_PS_9" />
+ </ObjectType>
+ <ObjectType Value="Pump">
+ <PropertyID Value="PROP_PU_0" />
+ <PropertyID Value="PROP_PU_1" />
+ <PropertyID Value="PROP_PU_2" />
+ <PropertyID Value="PROP_PU_3" />
+ <PropertyID Value="PROP_PU_4" />
+ <PropertyID Value="PROP_PU_5" />
+ </ObjectType>
+ <ObjectType Value="Reactor_Conversion">
+ <PropertyID Value="PROP_CR_0" />
+ <PropertyID Value="Calculation Mode" />
+ </ObjectType>
+ <ObjectType Value="Reactor_CSTR">
+ <PropertyID Value="Operating Pressure" />
+ <PropertyID Value="Liquid Level" />
+ <PropertyID Value="Height" />
+ <PropertyID Value="Minimum Pressure" />
+ <PropertyID Value="Initialize using Inlet Stream" />
+ <PropertyID Value="Reset Contents" />
+ <PropertyID Value="PROP_CS_0" />
+ <PropertyID Value="PROP_CS_1" />
+ <PropertyID Value="PROP_CS_2" />
+ <PropertyID Value="PROP_CS_3" />
+ <PropertyID Value="PROP_CS_4" />
+ <PropertyID Value="PROP_CS_5" />
+ <PropertyID Value="PROP_CS_6" />
+ <PropertyID Value="PROP_CS_7" />
+ <PropertyID Value="Calculation Mode" />
+ </ObjectType>
+ <ObjectType Value="Reactor_Equilibrium">
+ <PropertyID Value="PROP_EQ_0" />
+ <PropertyID Value="PROP_EQ_1" />
+ <PropertyID Value="Calculation Mode" />
+ <PropertyID Value="Initial Gibbs Energy" />
+ <PropertyID Value="Final Gibbs Energy" />
+ </ObjectType>
+ <ObjectType Value="Reactor_Gibbs">
+ <PropertyID Value="PROP_GR_0" />
+ <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" />
+ <PropertyID Value="Reset Contents" />
+ <PropertyID Value="PROP_PF_0" />
+ <PropertyID Value="PROP_PF_1" />
+ <PropertyID Value="PROP_PF_2" />
+ <PropertyID Value="PROP_PF_3" />
+ <PropertyID Value="PROP_PF_4" />
+ <PropertyID Value="PROP_PF_5" />
+ <PropertyID Value="PROP_PF_6" />
+ <PropertyID Value="PROP_PF_7" />
+ <PropertyID Value="PROP_PF_8" />
+ <PropertyID Value="PROP_PF_9" />
+ <PropertyID Value="Calculation Mode" />
+ </ObjectType>
+ <ObjectType Value="ReboiledAbsorber">
+ <PropertyID Value="PROP_RA_0" />
+ <PropertyID Value="PROP_RA_1" />
+ <PropertyID Value="PROP_RA_2" />
+ <PropertyID Value="PROP_RA_3" />
+ <PropertyID Value="PROP_RA_4" />
+ </ObjectType>
+ <ObjectType Value="Recycle">
+ <PropertyID Value="PROP_RY_0" />
+ <PropertyID Value="PROP_RY_1" />
+ <PropertyID Value="PROP_RY_2" />
+ <PropertyID Value="PROP_RY_3" />
+ <PropertyID Value="PROP_RY_4" />
+ <PropertyID Value="PROP_RY_5" />
+ <PropertyID Value="PROP_RY_6" />
+ </ObjectType>
+ <ObjectType Value="RefluxedAbsorber">
+ <PropertyID Value="PROP_RF_0" />
+ <PropertyID Value="PROP_RF_1" />
+ <PropertyID Value="PROP_RF_2" />
+ <PropertyID Value="PROP_RF_3" />
+ <PropertyID Value="PROP_RF_4" />
+ <PropertyID Value="PROP_RF_5" />
+ <PropertyID Value="PROP_RF_6" />
+ </ObjectType>
+ <ObjectType Value="ShortcutColumn">
+ <PropertyID Value="PROP_SC_0" />
+ <PropertyID Value="PROP_SC_1" />
+ <PropertyID Value="PROP_SC_2" />
+ <PropertyID Value="PROP_SC_3" />
+ <PropertyID Value="PROP_SC_4" />
+ <PropertyID Value="PROP_SC_5" />
+ <PropertyID Value="PROP_SC_6" />
+ <PropertyID Value="PROP_SC_7" />
+ <PropertyID Value="PROP_SC_8" />
+ <PropertyID Value="PROP_SC_9" />
+ <PropertyID Value="PROP_SC_10" />
+ <PropertyID Value="PROP_SC_11" />
+ <PropertyID Value="PROP_SC_12" />
+ <PropertyID Value="PROP_SC_13" />
+ <PropertyID Value="PROP_SC_14" />
+ </ObjectType>
+ <ObjectType Value="SolidsSeparator">
+ <PropertyID Value="PROP_SS_1" />
+ <PropertyID Value="PROP_SS_2" />
+ </ObjectType>
+ <ObjectType Value="Spec">
+ <PropertyID Value="SpecMin" />
+ <PropertyID Value="SpecMax" />
+ <PropertyID Value="Expression" />
+ </ObjectType>
+ <ObjectType Value="Splitter">
+ <PropertyID Value="PROP_SP_1" />
+ <PropertyID Value="PROP_SP_2" />
+ </ObjectType>
+ <ObjectType Value="Switch" />
+ <ObjectType Value="Tank">
+ <PropertyID Value="Liquid Level" />
+ <PropertyID Value="Height" />
+ <PropertyID Value="Initialize using Inlet Stream" />
+ <PropertyID Value="Reset Content" />
+ <PropertyID Value="PROP_TK_0" />
+ <PropertyID Value="PROP_TK_1" />
+ <PropertyID Value="PROP_TK_2" />
+ </ObjectType>
+ <ObjectType Value="Valve">
+ <PropertyID Value="PROP_VA_0" />
+ <PropertyID Value="PROP_VA_1" />
+ <PropertyID Value="PROP_VA_2" />
+ <PropertyID Value="PROP_VA_3" />
+ <PropertyID Value="PROP_VA_4" />
+ <PropertyID Value="PROP_VA_5" />
+ </ObjectType>
+ <ObjectType Value="Vessel">
+ <PropertyID Value="Vessel Orientation" />
+ <PropertyID Value="Operating Pressure" />
+ <PropertyID Value="Liquid Level" />
+ <PropertyID Value="Volume" />
+ <PropertyID Value="Height" />
+ <PropertyID Value="Minimum Pressure" />
+ <PropertyID Value="Initialize using Inlet Stream" />
+ <PropertyID Value="Reset Content" />
+ <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>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
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+ <FontStyle>Bold</FontStyle>
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+ </InputConnectors>
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+ <EnergyConnector>
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+ </GraphicObject>
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+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CompressorGraphic</Type>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <FontStyle>Bold</FontStyle>
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+ <Description>Adiabatic Compressor</Description>
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+ <ObjectType>Compressor</ObjectType>
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+ <ShapeOverride>DefaultShape</ShapeOverride>
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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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+ <FontStyle>Bold</FontStyle>
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+ <Active>true</Active>
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+ </InputConnectors>
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+ </OutputConnectors>
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+ <Description>Adiabatic Expander</Description>
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+ <ObjectType>Expander</ObjectType>
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+ </InputConnectors>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ </OutputConnectors>
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+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
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+ <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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+ </OutputConnectors>
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+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.RecycleGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Recycle Logical Op</Description>
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+ <ObjectType>OT_Recycle</ObjectType>
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+ <Status>Calculated</Status>
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+ <Height>20</Height>
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+ <Name>REC-7e353087-82f2-4985-ad91-120550d19d79</Name>
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+ </OutputConnectors>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <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>
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+ <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-c4d90083-5d18-465c-b70a-1e138e037b07</Name>
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+ <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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+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream Cooler</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Cooler</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>RESF-99f50845-cd88-4de0-b865-53da15112ae4</Name>
+ <Tag>C-01</Tag>
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+ <X>643.3372</X>
+ <Y>25.84323</Y>
+ <Selected>false</Selected>
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+ </OutputConnectors>
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+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.HeaterGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <FillColorDark>#ffffffff</FillColorDark>
+ <GradientColor1>#ffd3d3d3</GradientColor1>
+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream Heater</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Heater</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>AQ-ab8e71d7-ef71-4e8d-b843-9576e01d324f</Name>
+ <Tag>H-01</Tag>
+ <Width>25</Width>
+ <X>815.8832</X>
+ <Y>193.8775</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>0</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-f605b7a0-5204-4395-955c-a8584f619e92" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-8595d51c-1021-4001-b107-6f2795383db7" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-c2a9ba92-a2b5-42c2-98e1-52084ed0fd75" 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>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
+ <FillColor>#ffd3d3d3</FillColor>
+ <FillColorDark>#ffffffff</FillColorDark>
+ <GradientColor1>#ffd3d3d3</GradientColor1>
+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>true</IsEnergyStream>
+ <ObjectType>EnergyStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>EN-8595d51c-1021-4001-b107-6f2795383db7</Name>
+ <Tag>E-02</Tag>
+ <Width>20</Width>
+ <X>665.5807</X>
+ <Y>116.5459</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>0</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="RESF-99f50845-cd88-4de0-b865-53da15112ae4" AttachedFromConnIndex="-1" AttachedFromEnergyConn="False" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="AQ-ab8e71d7-ef71-4e8d-b843-9576e01d324f" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.TableGraphic</Type>
+ <Padding>4</Padding>
+ <TextColor>#ff000000</TextColor>
+ <BorderColor>#ff000000</BorderColor>
+ <TextColorDark>#fff5f5f5</TextColorDark>
+ <BorderColorDark>#fff5f5f5</BorderColorDark>
+ <HeaderText>PROPERTIES TABLE</HeaderText>
+ <ClipboardData>PROPERTIES TABLE
+E-01 Energy Flow 55.545 kW
+E-03 Energy Flow 124.131 kW
+CO-01 Outlet Pressure 19 bar
+TU-01 Outlet Pressure 1.01325 bar
+</ClipboardData>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#fffa8072</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
+ <FillColor>#ffd3d3d3</FillColor>
+ <FillColorDark>#ffffffff</FillColorDark>
+ <GradientColor1>#ffd3d3d3</GradientColor1>
+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>false</Calculated>
+ <Active>true</Active>
+ <Description></Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>GO_Table</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>NotCalculated</Status>
+ <AutoSize>true</AutoSize>
+ <Height>90</Height>
+ <IsConnector>false</IsConnector>
+ <Name>PROPERTYTABLE-d6e222cd-0187-41c6-b7b3-55c3935ad4cf</Name>
+ <Tag>PROPERTYTABLE-8f604bea-278e-483b-b23e-51df838e4d37</Tag>
+ <Width>175</Width>
+ <X>912.7932</X>
+ <Y>176.4752</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>0</DrawMode>
+ <InputConnectors />
+ <OutputConnectors />
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ <VisibleProperties>
+ <Object Value="EN-23c69939-c650-4cee-adc6-4c9e8ea9bcd8">
+ <PropertyID Value="PROP_ES_0" />
+ </Object>
+ <Object Value="EN-c4d90083-5d18-465c-b70a-1e138e037b07">
+ <PropertyID Value="PROP_ES_0" />
+ </Object>
+ <Object Value="COMP-d77c41c6-25bd-437b-b783-d585af4defe9">
+ <PropertyID Value="PROP_CO_4" />
+ </Object>
+ <Object Value="TURB-988fd0e2-d166-496a-b5d1-6d8e6abb8cf9">
+ <PropertyID Value="PROP_TU_4" />
+ </Object>
+ </VisibleProperties>
+ </GraphicObject>
+ </GraphicObjects>
+ <PropertyPackages>
+ <PropertyPackage>
+ <ID>PP-4969b289-f9ab-48e5-b866-1c3761d97dbb</ID>
+ <Type>DWSIM.Thermodynamics.PropertyPackages.RaoultPropertyPackage</Type>
+ <ComponentName>Raoult's Law</ComponentName>
+ <ComponentDescription>Reference Property Package (Ideal Gas/Solution).</ComponentDescription>
+ <Tag>Raoult's Law (1)</Tag>
+ <SingleCompoundCheckThreshold>0.99999</SingleCompoundCheckThreshold>
+ <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>
+ <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="" />
+ <Setting Name="PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases" Value="True" />
+ <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
+ </FlashSettings>
+ </PropertyPackage>
+ </PropertyPackages>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+ <Acentric_Factor>0.223621</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>124-38-9</CAS_Number>
+ <Chao_Seader_Acentricity>0.231</Chao_Seader_Acentricity>
+ <Chao_Seader_Liquid_Molar_Volume>37.2744</Chao_Seader_Liquid_Molar_Volume>
+ <Chao_Seader_Solubility_Parameter>0.0034785053748</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <Critical_Compressibility>0.274</Critical_Compressibility>
+ <Critical_Pressure>7383000</Critical_Pressure>
+ <Critical_Temperature>304.21</Critical_Temperature>
+ <Critical_Volume>0.094</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>9.019</EnthalpyOfFusionAtTf>
+ <Formula>CO2</Formula>
+ <HVap_A>21092000</HVap_A>
+ <HVap_B>0.35366</HVap_B>
+ <HVap_C>-0.46134</HVap_C>
+ <HVap_D>0.43554</HVap_D>
+ <HVap_E>0.037671</HVap_E>
+ <HVap_TMAX>304.21</HVap_TMAX>
+ <HVap_TMIN>216.58</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>909</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>28933</Ideal_Gas_Heat_Capacity_Const_A>
+ <Ideal_Gas_Heat_Capacity_Const_B>-494.28</Ideal_Gas_Heat_Capacity_Const_B>
+ <Ideal_Gas_Heat_Capacity_Const_C>10.658</Ideal_Gas_Heat_Capacity_Const_C>
+ <Ideal_Gas_Heat_Capacity_Const_D>-2.7375E-05</Ideal_Gas_Heat_Capacity_Const_D>
+ <Ideal_Gas_Heat_Capacity_Const_E>3.3268E-09</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>16</IdealgasCpEquation>
+ <IG_Enthalpy_of_Formation_25C>-8941.47854440518</IG_Enthalpy_of_Formation_25C>
+ <IG_Entropy_of_Formation_25C>0.0655416247361437</IG_Entropy_of_Formation_25C>
+ <IG_Gibbs_Energy_of_Formation_25C>-8961.01977982027</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>2.768</Liquid_Density_Const_A>
+ <Liquid_Density_Const_B>0.26212</Liquid_Density_Const_B>
+ <Liquid_Density_Const_C>304.21</Liquid_Density_Const_C>
+ <Liquid_Density_Const_D>0.2908</Liquid_Density_Const_D>
+ <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+ <Liquid_Density_Tmax>304.21</Liquid_Density_Tmax>
+ <Liquid_Density_Tmin>216.58</Liquid_Density_Tmin>
+ <Liquid_Heat_Capacity_Const_A>80592</Liquid_Heat_Capacity_Const_A>
+ <Liquid_Heat_Capacity_Const_B>108.83</Liquid_Heat_Capacity_Const_B>
+ <Liquid_Heat_Capacity_Const_C>-6.9126</Liquid_Heat_Capacity_Const_C>
+ <Liquid_Heat_Capacity_Const_D>0.059647</Liquid_Heat_Capacity_Const_D>
+ <Liquid_Heat_Capacity_Const_E>6.9922E-06</Liquid_Heat_Capacity_Const_E>
+ <Liquid_Heat_Capacity_Tmax>290</Liquid_Heat_Capacity_Tmax>
+ <Liquid_Heat_Capacity_Tmin>216.58</Liquid_Heat_Capacity_Tmin>
+ <Liquid_Thermal_Conductivity_Const_A>-0.24975</Liquid_Thermal_Conductivity_Const_A>
+ <Liquid_Thermal_Conductivity_Const_B>-55.106</Liquid_Thermal_Conductivity_Const_B>
+ <Liquid_Thermal_Conductivity_Const_C>0.41735</Liquid_Thermal_Conductivity_Const_C>
+ <Liquid_Thermal_Conductivity_Const_D>-0.0051067</Liquid_Thermal_Conductivity_Const_D>
+ <Liquid_Thermal_Conductivity_Const_E>2.0157E-06</Liquid_Thermal_Conductivity_Const_E>
+ <Liquid_Thermal_Conductivity_Tmax>300</Liquid_Thermal_Conductivity_Tmax>
+ <Liquid_Thermal_Conductivity_Tmin>216.58</Liquid_Thermal_Conductivity_Tmin>
+ <Liquid_Viscosity_Const_A>-7.7022</Liquid_Viscosity_Const_A>
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+ <Liquid_Viscosity_Const_C>0.38094</Liquid_Viscosity_Const_C>
+ <Liquid_Viscosity_Const_D>-4.018E-05</Liquid_Viscosity_Const_D>
+ <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+ <LiquidDensityEquation>105</LiquidDensityEquation>
+ <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
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+ <LiquidViscosityEquation>101</LiquidViscosityEquation>
+ <Molar_Weight>44.0095</Molar_Weight>
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+ <MolarVolume_k3i>0</MolarVolume_k3i>
+ <MolarVolume_v2i>0</MolarVolume_v2i>
+ <MolarVolume_v3i>0</MolarVolume_v3i>
+ <Name>Carbon dioxide</Name>
+ <NegativeIon></NegativeIon>
+ <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+ <Normal_Boiling_Point>0</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>O=C=O</SMILES>
+ <Solid_Density_Const_A>42.04</Solid_Density_Const_A>
+ <Solid_Density_Const_B>-0.034421</Solid_Density_Const_B>
+ <Solid_Density_Const_C>-0.0002847</Solid_Density_Const_C>
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+ <Solid_Density_Tmax>216.58</Solid_Density_Tmax>
+ <Solid_Density_Tmin>143.1</Solid_Density_Tmin>
+ <Solid_Heat_Capacity_Const_A>-18283</Solid_Heat_Capacity_Const_A>
+ <Solid_Heat_Capacity_Const_B>1360.3</Solid_Heat_Capacity_Const_B>
+ <Solid_Heat_Capacity_Const_C>-12.153</Solid_Heat_Capacity_Const_C>
+ <Solid_Heat_Capacity_Const_D>0.051584</Solid_Heat_Capacity_Const_D>
+ <Solid_Heat_Capacity_Const_E>-7.6997E-05</Solid_Heat_Capacity_Const_E>
+ <Solid_Heat_Capacity_Tmax>216.58</Solid_Heat_Capacity_Tmax>
+ <Solid_Heat_Capacity_Tmin>25</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>-0.011629</Surface_Tension_Const_A>
+ <Surface_Tension_Const_B>-183.67</Surface_Tension_Const_B>
+ <Surface_Tension_Const_C>0.069773</Surface_Tension_Const_C>
+ <Surface_Tension_Const_D>-0.012408</Surface_Tension_Const_D>
+ <Surface_Tension_Const_E>-1.8232E-06</Surface_Tension_Const_E>
+ <Surface_Tension_Tmax>304.21</Surface_Tension_Tmax>
+ <Surface_Tension_Tmin>216.58</Surface_Tension_Tmin>
+ <SurfaceTensionEquation>16</SurfaceTensionEquation>
+ <TemperatureOfFusion>216.58</TemperatureOfFusion>
+ <UNIQUAC_Q>1.292</UNIQUAC_Q>
+ <UNIQUAC_R>1.2986</UNIQUAC_R>
+ <Vapor_Pressure_Constant_A>95.478</Vapor_Pressure_Constant_A>
+ <Vapor_Pressure_Constant_B>-4070</Vapor_Pressure_Constant_B>
+ <Vapor_Pressure_Constant_C>-12.07</Vapor_Pressure_Constant_C>
+ <Vapor_Pressure_Constant_D>2.9505E-05</Vapor_Pressure_Constant_D>
+ <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+ <Vapor_Pressure_TMAX>304.21</Vapor_Pressure_TMAX>
+ <Vapor_Pressure_TMIN>216.4</Vapor_Pressure_TMIN>
+ <Vapor_Thermal_Conductivity_Const_A>5.804</Vapor_Thermal_Conductivity_Const_A>
+ <Vapor_Thermal_Conductivity_Const_B>-0.44522</Vapor_Thermal_Conductivity_Const_B>
+ <Vapor_Thermal_Conductivity_Const_C>794.13</Vapor_Thermal_Conductivity_Const_C>
+ <Vapor_Thermal_Conductivity_Const_D>2139600</Vapor_Thermal_Conductivity_Const_D>
+ <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
+ <Vapor_Thermal_Conductivity_Tmax>1500</Vapor_Thermal_Conductivity_Tmax>
+ <Vapor_Thermal_Conductivity_Tmin>180</Vapor_Thermal_Conductivity_Tmin>
+ <Vapor_Viscosity_Const_A>2.2464E-06</Vapor_Viscosity_Const_A>
+ <Vapor_Viscosity_Const_B>0.45495</Vapor_Viscosity_Const_B>
+ <Vapor_Viscosity_Const_C>292.64</Vapor_Viscosity_Const_C>
+ <Vapor_Viscosity_Const_D>1669.1</Vapor_Viscosity_Const_D>
+ <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+ <Vapor_Viscosity_Tmax>1900</Vapor_Viscosity_Tmax>
+ <Vapor_Viscosity_Tmin>170</Vapor_Viscosity_Tmin>
+ <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+ <VaporPressureEquation>101</VaporPressureEquation>
+ <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+ <VaporViscosityEquation>102</VaporViscosityEquation>
+ <Z_Rackett>0.270937</Z_Rackett>
+ <FullerDiffusionVolume>26.9</FullerDiffusionVolume>
+ <LennardJonesDiameter>4.011624E-10</LennardJonesDiameter>
+ <LennardJonesEnergy>187.9268</LennardJonesEnergy>
+ <Parachor>0.0132</Parachor>
+ <Tag></Tag>
+ <COSTALD_SRK_Acentric_Factor>0.231</COSTALD_SRK_Acentric_Factor>
+ <COSTALD_Characteristic_Volume>0.104698</COSTALD_Characteristic_Volume>
+ <IsSolid>false</IsSolid>
+ <DynamicProperties />
+ <UNIFACGroups />
+ <MODFACGroups />
+ <NISTMODFACGroups />
+ <Elements>
+ <Item Name="C" Value="1" />
+ <Item Name="O" Value="2" />
+ </Elements>
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+ <Acentric_Factor>0.364300568809497</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>7789-20-0</CAS_Number>
+ <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
+ <Chao_Seader_Liquid_Molar_Volume>0</Chao_Seader_Liquid_Molar_Volume>
+ <Chao_Seader_Solubility_Parameter>0</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments>Compound converted from CoolProp data using CoolProp v6.0.0
+ALIASES
+D2O, HEAVYWATER
+COOLPROP DATA AVAILABILITY
+Ideal Gas Cp: OK
+Vapor Viscosity: OK
+Vapor Thermal Conductivity: OK
+Vapor Pressure: OK
+Liquid Density: OK
+Liquid Viscosity: OK
+Liquid Thermal Conductivity: OK
+Liquid Heat Capacity: OK
+BIBLIOGRAPHY
+http://www.coolprop.org/fluid_properties/PurePseudoPure.html#list-of-fluids
+FITTING INPUT
+Temperature Points for Liquid Properties (K): 543 547 551 555 559 563 567 571 575 579 583 587 591 595 599 603 607 611 615 619 623 627 631 635 639 643 647 651 655 659 663 667 671 675 679 683 687 691 695 699 703 707 711 715 719 723 727 731 735 739 743 747 751 755 759 763 767 771 775 779 783 787 791 795 799 803 807 811 815 819 823 375 379 383 387 391 395 399 403 407 411 415 419 423 427 431 435 439 443 447 451 455 459 463 467 471 475 479 483 487 491 495 499 503 507 511 515 519 523 527 531 535 539
+Liquid Density Data Points (kg/m3): 992.848708417 1105.51970841 1105.63480981 1105.73029166 1105.80666805 1105.86443016 1105.90404744 1105.92596873 1105.93062338 1105.91842227 1105.88975876 1105.84500966 1105.78453606 1105.70868421 1105.61778626 1105.51216104 1105.39211473 1105.25794152 1105.10992427 1104.94833503 1104.77343566 1104.58547830 1104.38470590 1104.17135266 1103.94564446 1103.70779928 1103.45802761 1103.19653275 1102.92351122 1102.63915307 1102.34364214 1102.03715639 1101.71986817 1101.39194445 1101.05354710 1100.70483305 1100.34595459 1099.97705951 1099.59829131 1099.20978938 1098.81168917 1098.40412237 1097.98721701 1097.56109765 1097.12588553 1096.68169863 1096.22865185 1095.76685713 1095.29642349 1094.81745722 1094.33006191 1093.83433860 1093.33038582 1092.81829968 1092.29817397 1091.77010025 1091.23416785 1090.69046403 1090.13907396 1089.58008084 1089.01356594 1088.43960864 1087.85828650 1087.26967532 1086.67384915 1086.07088037 1085.46083972 1084.84379636 1084.21981785 1083.58897029 1082.95131824 1082.30692484 1081.65585182 1080.99815951 1080.33390688 1079.66315159 1078.98595000 1078.30235718 1077.61242698 1076.91621201 1076.21376367 1075.50513221 1074.79036671 1074.06951512 1073.34262426 1072.60973987 1071.87090661 1071.12616807 1070.37556680 1069.61914434 1068.85694118 1068.08899687 1067.31534991 1066.53603790 1065.75109742 1064.96056417 1064.16447288 1063.36285737
+Liquid Viscosity Data Points (Pa.s): 0.00126974584917 0.00208156052335 0.00200595006664 0.00193466096043 0.0018673691699 0.0018037800413 0.00174362521739 0.00168665991791 0.00163266053741 0.0015814225194 0.0015327584716 0.00148649649197 0.00144247867937 0.00140055980628 0.00136060613395 0.00132249435308 0.0012861106351 0.00125134978143 0.00121811445926 0.00118631451411 0.00115586635074 0.00112669237454 0.00109872048715 0.00107188363011 0.00104611937181 0.00102136953274 0.000997579845465 0.000974699645486 0.000952681589926 0.000931481401277 0.000911057633673 0.000891371459491 0.000872386474298 0.000854068518388 0.000836385513328 0.000819307312094 0.000802805561545 0.000786853576086 0.00077142622151 0.000756499808098 0.000742051992142 0.000728061685162 0.000714508970138 0.000701375024136 0.000688642046808 0.000676293194237 0.0006643125177 0.000652684906931 0.000641396037507 0.000630432322034 0.000619780864814 0.000609429419717 0.00059936635101 0.000589580596896 0.000580061635569 0.000570799453576 0.000561784516318 0.000553007740525 0.000544460468553 0.000536134444376 0.000528021791137 0.000520114990152 0.000512406861256 0.000504890544397 0.00049755948239 0.000490407404745 0.000483428312495 0.000476616463956 0.000469966361354 0.000463472738257 0.000457130547761 0.000450934951373 0.000444881308554 0.000438965166868 0.000433182252706 0.000427528462538 0.000421999854666 0.000416592641443 0.000411303181931 0.000406127974965 0.000401063652597 0.000396106973907 0.000391254819146 0.000386504184194 0.000381852175315 0.000377296004197 0.000372832983243 0.000368460521118 0.000364176118523 0.000359977364185 0.000355861931056 0.000351827572705 0.00034787211989 0.0003439934773 0.000340189620464 0.00033645859281 0.000332798502863 0.00032920752159
+Liquid Thermal Conductivity Data Points (W/[m.K]): 0.302917832381 564.682121665 566.355602504 568.001412655 569.620046729 571.211977909 572.777659059 574.317523798 575.831987520 577.321448369 578.786288175 580.226873337 581.643555662 583.036673168 584.406550834 585.753501321 587.077825645 588.379813816 589.659745446 590.917890316 592.154508913 593.369852942 594.564165798 595.737683024 596.890632729 598.023235997 599.135707255 600.228254636 601.301080311 602.354380806 603.388347297 604.403165892 605.399017896 606.376080057 607.334524800 608.274520452 609.196231446 610.099818517 610.985438890 611.853246449 612.703391907 613.536022958 614.351284419 615.149318376 615.930264307 616.694259206 617.441437700 618.171932156 618.885872787 619.583387744 620.264603212 620.929643493 621.578631092 622.211686789 622.828929715 623.430477418 624.016445932 624.586949834 625.142102303 625.682015177 626.206799001 626.716563078 627.211415514 627.691463261 628.156812159 628.607566975 629.043831439 629.465708278 629.873299247 630.266705163 630.646025934 631.011360581 631.362807269 631.700463330 632.024425285 632.334788863 632.631649025 632.915099983 633.185235211 633.442147472 633.685928822 633.916670634 634.134463606 634.339397774 634.531562525 634.711046606 634.877938135 635.032324610 635.174292916 635.303929333 635.421319542 635.526548634 635.619701110 635.700860891 635.770111318 635.827535158 635.873214605 635.907231283
+Liquid Heat Capacity Data Points (kJ/[kg.K]): 3.5353262925 4.26909444466 4.26057239073 4.25277875578 4.24566559183 4.23918750572 4.23330154497 4.22796708712 4.22314573279 4.21880120258 4.21489923778 4.21140750487 4.20829550381 4.20553448009 4.20309734031 4.20095857142 4.19909416322 4.19748153440 4.19609946156 4.19492801153 4.19394847651 4.19314331222 4.19249607869 4.19199138381 4.19161482935 4.19135295945 4.19119321148 4.19112386913 4.19113401766 4.19121350121 4.19135288213 4.19154340214 4.19177694539 4.19204600323 4.19234364063 4.19266346421 4.19299959184 4.19334662364 4.19369961444 4.19405404754 4.19440580978 4.19475116784 4.19508674567 4.19540950314 4.19571671564 4.19600595478 4.19627507010 4.19652217161 4.19674561335 4.19694397770 4.19711606056 4.19726085732 4.19737754952 4.19746549227 4.19752420230 4.19755334670 4.19755273225 4.19752229534 4.19746209243 4.19737229106 4.19725316139 4.19710506814 4.1969284631 4.19672387797 4.19649191769 4.19623325412 4.19594862011 4.19563880393 4.19530464404 4.19494702415 4.19456686863 4.19416513818 4.19374282578 4.19330095291 4.19284056599 4.19236273309 4.19186854084 4.19135909153 4.19083550048 4.19029889348 4.18975040456 4.18919117376 4.18862234521 4.18804506526 4.18746048077 4.18686973761 4.18627397916 4.18567434503 4.18507196984 4.18446798213 4.18386350339 4.18325964709 4.18265751793 4.18205821107 4.18146281149 4.18087239342 4.18028801979 4.17971074184
+Vapor Pressure Data Points (Pa): 663.535912910 713.524967110 766.820568560 823.609221521 884.086003652 948.454790984 1016.92857419 1089.72972526 1167.09033559 1249.25249415 1336.46858527 1429.00162980 1527.12557092 1631.12561502 1741.29854190 1857.95305194 1981.41007106 2112.00309737 2250.07854476 2395.99607894 2550.12896342 2712.86439954 2884.60389532 3065.76359232 3256.77464152 3458.08355548 3670.15256220 3893.45997245 4128.50053959 4375.78583873 4635.84460767 4909.22312732 5196.48561373 5498.21454939 5815.01106688 6147.49533960 6496.30693475 6862.10517079 7245.56954120 7647.40003022 8068.31751238 8509.06412340 8970.40362564 9453.12177290 9958.02669127 10485.9492397 11037.7433797 11614.2865336 12216.4799493 12845.2490758 13501.5439136 14186.3393505 14900.6355562 15645.4583037 16421.8593395 17230.9167144 18073.7351417 18951.4463312 19865.2093254 20816.2108455 21805.6656077 22834.8166682 23904.9357288 25017.3234711 26173.3098788 27374.2545088 28621.5468711 29916.6066698 31260.8841295 32655.8602834 34103.0472771 35603.9886285 37160.2595410 38773.4671549 40445.2508264 42177.2824015 43971.2664649 45828.9406032 47752.0756519 49742.4759496 51801.9795694 53932.4585505 56135.8191412 58414.0020090 60768.9824669 63202.7706830 65717.4118886 68314.9865773 70997.6107016 73767.4358662 76626.6495100 79577.4750753 82622.1721973 85763.0368608 89002.4015611 92342.6354580 95786.1445374
+Temperature Points for Vapor Properties (K): 277 278 279 280 281 282 283 284 285 286 287 288 289 290 291 292 293 294 295 296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 314 315 316 317 318 319 320 321 322 323 324 325 326 327 328 329 330 331 332 333 334 335 336 337 338 339 340 341 342 343 344 345 346 347 348 349 350 351 352 353 354 355 356 357 358 359 360 361 362 363 364 365 366 367 368 369 370 371 372 373
+Ideal Gas Heat Capacity Data Points (kJ/[kg.K]): 1.89152269599 1.89481748651 1.89811940066 1.90142830100 1.90474404528 1.90806648643 1.91139547253 1.91473084691 1.91807244815 1.92142011020 1.92477366244 1.92813292985 1.93149773308 1.93486788862 1.93824320895 1.94162350271 1.94500857485 1.94839822683 1.95179225682 1.95519045983 1.95859262798 1.96199855066 1.96540801471 1.96882080468 1.97223670297 1.97565549010 1.97907694484 1.98250084446 1.98592696492 1.98935508106 1.99278496679 1.99621639530 1.99964913921 2.00308297082 2.00651766221 2.00995298548 2.01338871287 2.01682461698 2.02026047088 2.02369604829 2.02713112373 2.03056547268 2.03399887168 2.03743109850 2.04086193226 2.04429115355 2.04771854457 2.05114388918 2.05456697311 2.05798758397 2.06140551139 2.06482054711 2.06823248507 2.07164112147 2.07504625489 2.07844768631 2.08184521921 2.08523865966 2.08862781629 2.09201250045 2.0953925262 2.09876771035 2.10213787254 2.10550283525 2.10886242383 2.11221646658 2.11556479470 2.11890724237 2.12224364676 2.12557384804 2.12889768938 1.76116430625 1.76403426742 1.76692031989 1.76982180634 1.77273811773 1.77566869088 1.77861300611 1.78157058475 1.78454098674 1.78752380822 1.79051867909 1.79352526076 1.79654324373 1.79957234544 1.80261230807 1.80566289639 1.80872389580 1.81179511032 1.81487636076 1.81796748293 1.82106832593 1.82417875054 1.82729862775 1.83042783724 1.83356626612 1.83671380761 1.83987035988 1.84303582496 1.84621010774 1.84939311499 1.85258475454 1.85578493446 1.85899356235 1.86221054472 1.86543578633 1.86866918974 1.87191065478 1.87516007818 1.87841735317 1.88168236921 1.88495501169 1.88823516173
+Vapor Viscosity Data Points (Pa.s): 1.9582305556e-05 1.97508649483e-05 1.99195495235e-05 2.00883502445e-05 2.02572583201e-05 2.04262651968e-05 2.05953625519e-05 2.07645422852e-05 2.09337965128e-05 2.11031175602e-05 2.12724979558e-05 2.14419304248e-05 2.16114078836e-05 2.17809234336e-05 2.19504703565e-05 2.21200421084e-05 2.22896323154e-05 2.24592347682e-05 2.26288434181e-05 2.27984523721e-05 2.29680558887e-05 2.31376483737e-05 2.33072243766e-05 2.3476778586e-05 2.36463058267e-05 2.38158010554e-05 2.39852593578e-05 2.41546759449e-05 2.43240461497e-05 2.44933654243e-05 2.46626293367e-05 2.48318335679e-05 2.50009739092e-05 2.5170046259e-05 2.53390466206e-05 2.55079710994e-05 2.56768159001e-05 2.5845577325e-05 2.60142517706e-05 2.61828357264e-05 2.63513257718e-05 2.65197185743e-05 2.66880108872e-05 2.6856199548e-05 2.70242814758e-05 2.71922536696e-05 2.73601132068e-05 2.75278572407e-05 2.76954829991e-05 2.78629877825e-05 2.80303689625e-05 2.819762398e-05 2.83647503435e-05 2.85317456279e-05 2.86986074726e-05 2.88653335804e-05 2.90319217156e-05 2.9198369703e-05 2.93646754263e-05 2.95308368268e-05 2.96968519022e-05 2.98627187051e-05 3.00284353421e-05 3.01939999722e-05 3.0359410806e-05 3.05246661042e-05 3.06897641768e-05 3.08547033818e-05 3.10194821239e-05 3.11840988542e-05 3.13485520684e-05 1.27900067883e-05 1.29397236156e-05 1.30903973664e-05 1.32419873317e-05 1.33944548384e-05 1.35477630985e-05 1.37018770746e-05 1.38567633564e-05 1.40123900494e-05 1.4168726673e-05 1.43257440684e-05 1.44834143137e-05 1.46417106463e-05 1.48006073926e-05 1.49600799023e-05 1.51201044888e-05 1.5280658374e-05 1.54417196377e-05 1.56032671706e-05 1.57652806304e-05 1.59277404026e-05 1.60906275621e-05 1.62539238392e-05 1.64176115874e-05 1.65816737531e-05 1.67460938477e-05 1.69108559216e-05 1.70759445396e-05 1.72413447584e-05 1.74070421044e-05 1.75730225546e-05 1.77392725167e-05 1.79057788121e-05 1.80725286589e-05 1.8239509656e-05 1.84067097684e-05 1.85741173131e-05 1.87417209458e-05 1.89095096482e-05 1.90774727164e-05 1.92455997494e-05 1.94138806382e-05
+Vapor Thermal Conductivity Data Points (W/[m.K]): 0.0391444156882 0.0395448887219 0.0399474550128 0.040352124756 0.0407589073497 0.0411678113914 0.0415788446763 0.0419920141974 0.0424073261465 0.0428247859181 0.043244398113 0.0436661665446 0.0440900942454 0.0445161834752 0.0449444357301 0.0453748517521 0.0458074315399 0.0462421743603 0.0466790787602 0.0471181425796 0.0475593629641 0.0480027363794 0.0484482586248 0.0488959248483 0.0493457295606 0.0497976666509 0.0502517294021 0.050707910506 0.0511662020795 0.0516265956798 0.052089082321 0.0525536524895 0.0530202961604 0.0534890028132 0.0539597614481 0.0544325606021 0.0549073883642 0.0553842323919 0.0558630799272 0.0563439178112 0.0568267325006 0.0573115100826 0.0577982362903 0.0582868965176 0.0587774758343 0.0592699590005 0.0597643304817 0.0602605744624 0.0607586748608 0.0612586153421 0.061760379333 0.0622639500343 0.0627693104346 0.0632764433235 0.0637853313038 0.0642959568043 0.0648083020925 0.0653223492857 0.0658380803639 0.0663554771803 0.0668745214737 0.0673951948787 0.0679174789368 0.0684413551072 0.0689668047769 0.069493809271 0.0700223498621 0.0705524077807 0.0710839642238 0.0716170003645 0.0721514973607 0.0240004616373 0.0243275019638 0.0246561039348 0.0249862499162 0.0253179264823 0.0256511241026 0.0259858368422 0.0263220620728 0.0266598001958 0.0269990543782 0.0273398303004 0.0276821359165 0.0280259812262 0.0283713780592 0.028718339871 0.02906688155 0.0294170192359 0.0297687701484 0.0301221524271 0.0304771849804 0.0308338873447 0.0311922795526 0.03155238201 0.0319142153817 0.0322778004849 0.0326431581909 0.0330103093334 0.0333792746244 0.0337500745766 0.0341227294321 0.0344972590968 0.0348736830806 0.0352520204434 0.0356322897453 0.0360145090021 0.0363986956456 0.036784866487 0.0371730376855 0.0375632247199 0.037955442364 0.0383497046651 0.0387460249257
+REGRESSION FITNESS
+Ideal Gas Heat Capacity: 1.0
+Vapor Viscosity: 1.0
+Vapor Thermal Conductivity: 1.0
+Vapor Pressure: -1860.94687171
+Liquid Density: 1.0
+Liquid Viscosity: 0.999999395886
+Liquid Thermal Conductivity: 1.0
+Liquid Heat Capacity: 1.0
+TEMPERATURE AND PRESSURE LIMITS
+Minimum Temperature (K): 276.969
+Maximum Temperature (K): 825.0
+Minimum Pressure (Pa): 662.037140022
+Maximum Pressure (Pa): 1000000000.0
+MISCELLANEOUS
+Temperature of Fusion is actually the Triple Point Temperature as provided by CoolProp.
+Normal Boiling Point is calculated at 1 atm or at the minimum CoolProp pressure for the compound if higher.</Comments>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <Critical_Compressibility>0.227763579633536</Critical_Compressibility>
+ <Critical_Pressure>21672051.4798282</Critical_Pressure>
+ <Critical_Temperature>643.847</Critical_Temperature>
+ <Critical_Volume>0.056257049711542</Critical_Volume>
+ <CurrentDB>CoolProp</CurrentDB>
+ <Dipole_Moment>0</Dipole_Moment>
+ <Electrolyte_Cp0>0</Electrolyte_Cp0>
+ <Electrolyte_DelGF>0</Electrolyte_DelGF>
+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
+ <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
+ <Formula>D2O1</Formula>
+ <HVap_A>2076.26608604414</HVap_A>
+ <HVap_B>0</HVap_B>
+ <HVap_C>0</HVap_C>
+ <HVap_D>0</HVap_D>
+ <HVap_E>0</HVap_E>
+ <HVap_TMAX>0</HVap_TMAX>
+ <HVap_TMIN>0</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>300024</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>1.49006521396444</Ideal_Gas_Heat_Capacity_Const_A>
+ <Ideal_Gas_Heat_Capacity_Const_B>0.000666753663197295</Ideal_Gas_Heat_Capacity_Const_B>
+ <Ideal_Gas_Heat_Capacity_Const_C>1.36222899742311E-07</Ideal_Gas_Heat_Capacity_Const_C>
+ <Ideal_Gas_Heat_Capacity_Const_D>0</Ideal_Gas_Heat_Capacity_Const_D>
+ <Ideal_Gas_Heat_Capacity_Const_E>0</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>3</IdealgasCpEquation>
+ <IG_Enthalpy_of_Formation_25C>0</IG_Enthalpy_of_Formation_25C>
+ <IG_Entropy_of_Formation_25C>0</IG_Entropy_of_Formation_25C>
+ <IG_Gibbs_Energy_of_Formation_25C>0</IG_Gibbs_Energy_of_Formation_25C>
+ <InChI></InChI>
+ <Ion_CpAq_a>0</Ion_CpAq_a>
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diff --git a/Formic_Acid_Production_In_A_Reactive_Dividing_Wall_Column_By_Mr_Luis_Bayas_/user_defined_compound/1.json b/Formic_Acid_Production_In_A_Reactive_Dividing_Wall_Column_By_Mr_Luis_Bayas_/user_defined_compound/1.json
new file mode 100644
index 0000000..80e0ab6
--- /dev/null
+++ b/Formic_Acid_Production_In_A_Reactive_Dividing_Wall_Column_By_Mr_Luis_Bayas_/user_defined_compound/1.json
@@ -0,0 +1,204 @@
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+ "BO_PNA_N": 0.0,
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+ "Chao_Seader_Liquid_Molar_Volume": 46.3,
+ "Chao_Seader_Solubility_Parameter": 14.26,
+ "Charge": 0,
+ "ChemicalStructure": "",
+ "Comments": "",
+ "CompCreatorStudyFile": "C:\\Users\\DELL\\Documents\\IQ\\Asesoría\\Tesis\\Formic Acid.dwcsd2",
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+ "Critical_Pressure": 7587806.09,
+ "Critical_Temperature": 588.0,
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+ "Formula": "O2H2C",
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+ "Liquid_Thermal_Conductivity_Const_B": 0.0,
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+ "NegativeIon": "",
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+ "PF_Tv2": null,
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+ "PF_v2": null,
+ "PF_vA": null,
+ "PF_vB": null,
+ "PF_Watson_K": null,
+ "PositiveIon": "",
+ "PositiveIonStoichCoeff": 0,
+ "PR_Volume_Translation_Coefficient": 0.0,
+ "SMILES": "C(=O)O",
+ "Solid_Density_Const_A": 34.2478414382447,
+ "Solid_Density_Const_B": -0.005,
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+ "SolidDensityAtTs": 0.0,
+ "SolidDensityEquation": "2",
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+ "SolidTs": 0.0,
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+ "Surface_Tension_Const_E": 0.0,
+ "Surface_Tension_Tmax": 0.0,
+ "Surface_Tension_Tmin": 0.0,
+ "SurfaceTensionEquation": "",
+ "TemperatureOfFusion": 203.85,
+ "UNIQUAC_Q": 0.0,
+ "UNIQUAC_R": 0.0,
+ "Vapor_Pressure_Constant_A": 0.0,
+ "Vapor_Pressure_Constant_B": 0.0,
+ "Vapor_Pressure_Constant_C": 0.0,
+ "Vapor_Pressure_Constant_D": 0.0,
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+ "Vapor_Pressure_TMIN": 0.0,
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+ "Vapor_Thermal_Conductivity_Const_B": 0.0,
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+ "Vapor_Thermal_Conductivity_Const_D": 0.0,
+ "Vapor_Thermal_Conductivity_Const_E": 0.0,
+ "Vapor_Thermal_Conductivity_Tmax": 0.0,
+ "Vapor_Thermal_Conductivity_Tmin": 0.0,
+ "Vapor_Viscosity_Const_A": 0.0,
+ "Vapor_Viscosity_Const_B": 0.0,
+ "Vapor_Viscosity_Const_C": 0.0,
+ "Vapor_Viscosity_Const_D": 0.0,
+ "Vapor_Viscosity_Const_E": 0.0,
+ "Vapor_Viscosity_Tmax": 0.0,
+ "Vapor_Viscosity_Tmin": 0.0,
+ "VaporizationEnthalpyEquation": "",
+ "VaporPressureEquation": "0",
+ "VaporThermalConductivityEquation": "",
+ "VaporViscosityEquation": "",
+ "Z_Rackett": 0.22,
+ "Elements": {
+ "C": 1,
+ "H": 2,
+ "O": 2
+ },
+ "MODFACGroups": {
+ "43": "1"
+ },
+ "NISTMODFACGroups": {
+ "43": "1"
+ },
+ "UNIFACGroups": {
+ "44": "1"
+ },
+ "FullerDiffusionVolume": 0.0,
+ "LennardJonesDiameter": 0.0,
+ "LennardJonesEnergy": 0.0,
+ "Parachor": 0.0,
+ "Tag": "",
+ "ExtraProperties": {},
+ "COSTALD_SRK_Acentric_Factor": 0.0,
+ "COSTALD_Characteristic_Volume": 0.0,
+ "IsSolid": false
+} \ No newline at end of file
diff --git a/Kalina_Cycle_With_Double_Turbine_And_Reheating_By_Mr_Francis_Parra/Abstract.pdf b/Kalina_Cycle_With_Double_Turbine_And_Reheating_By_Mr_Francis_Parra/Abstract.pdf
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diff --git a/Kalina_Cycle_With_Double_Turbine_And_Reheating_By_Mr_Francis_Parra/Flowsheet.dwxmz b/Kalina_Cycle_With_Double_Turbine_And_Reheating_By_Mr_Francis_Parra/Flowsheet.dwxmz
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generated by cgit (git 2.34.1) at 2024-12-19 15:34:08 +0000