diff options
author | Sashi20 | 2025-03-16 00:20:14 +0550 |
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committer | Sashi20 | 2025-03-16 00:20:14 +0550 |
commit | a1cb225f88d42685dc1ee406dc971e33818fb218 (patch) | |
tree | 1e6075d3f96d7a324bef4e2579792468b3a592b4 | |
parent | e29baed6edb255d1d2012aff9212dc247d129c5d (diff) | |
download | DWSIM-Flowsheets-master.tar.gz DWSIM-Flowsheets-master.tar.bz2 DWSIM-Flowsheets-master.zip |
A Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/abstract.pdf
A Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/flowsheet.dwxmz
A Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/Abstract_DWSIM.pdf
A Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/B6_Final.dwxmz
A Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf
A Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml
A Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Abstract_DiethyleneGlycol.pdf
A Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Diethylene_Glycol.dwxmz
-rw-r--r-- | Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/abstract.pdf | bin | 0 -> 552960 bytes | |||
-rw-r--r-- | Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/flowsheet.dwxmz | bin | 0 -> 53462 bytes | |||
-rw-r--r-- | Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/Abstract_DWSIM.pdf | bin | 0 -> 217267 bytes | |||
-rw-r--r-- | Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/B6_Final.dwxmz | bin | 0 -> 294256 bytes | |||
-rw-r--r-- | Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf | bin | 0 -> 238630 bytes | |||
-rw-r--r-- | Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml | 9016 | ||||
-rw-r--r-- | Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Abstract_DiethyleneGlycol.pdf | bin | 0 -> 308684 bytes | |||
-rw-r--r-- | Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Diethylene_Glycol.dwxmz | bin | 0 -> 528676 bytes |
8 files changed, 9016 insertions, 0 deletions
diff --git a/Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/abstract.pdf b/Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/abstract.pdf Binary files differnew file mode 100644 index 0000000..54588c7 --- /dev/null +++ b/Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/abstract.pdf diff --git a/Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/flowsheet.dwxmz b/Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/flowsheet.dwxmz Binary files differnew file mode 100644 index 0000000..a22e4ec --- /dev/null +++ b/Energy_Generation_By_Combustion_Of_Methane_By_Mr_Dylan_Muli_Kyeni/flowsheet.dwxmz diff --git a/Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/Abstract_DWSIM.pdf b/Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/Abstract_DWSIM.pdf Binary files differnew file mode 100644 index 0000000..d76b57e --- /dev/null +++ b/Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/Abstract_DWSIM.pdf diff --git a/Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/B6_Final.dwxmz b/Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/B6_Final.dwxmz Binary files differnew file mode 100644 index 0000000..9ddeae3 --- /dev/null +++ b/Ethylene_Oxide_Production_From_Styrene_By_Mr_Paresh_Rathod/B6_Final.dwxmz diff --git a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf b/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf Binary files differnew file mode 100644 index 0000000..f162bbf --- /dev/null +++ b/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf diff --git a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml b/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml new file mode 100644 index 0000000..ecd62fd --- /dev/null +++ b/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml @@ -0,0 +1,9016 @@ +<?xml version="1.0" encoding="utf-8"?>
+<DWSIM_Simulation_Data>
+ <GeneralInfo>
+ <BuildVersion>8.8.3.0</BuildVersion>
+ <BuildDate>2000-01-04T00:00:00</BuildDate>
+ <OSInfo>Microsoft Windows 11 Home, Version 10.0.26100.0, Win32NT Platform</OSInfo>
+ <SavedOn>2025-03-08T17:25:56.5010584+05:30</SavedOn>
+ <SavedFromClassicUI>true</SavedFromClassicUI>
+ </GeneralInfo>
+ <SimulationObjects>
+ <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>873.15</OutletTemperature>
+ <CalcMode>OutletTemperature</CalcMode>
+ <DeltaP>200000</DeltaP>
+ <DeltaT>575</DeltaT>
+ <DeltaQ>3932.39694266773</DeltaQ>
+ <HeatDuty>3932.39694266773</HeatDuty>
+ <Efficiency>100</Efficiency>
+ <PressureDrop>200000</PressureDrop>
+ <TemperatureChange>575</TemperatureChange>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ParticleSizeDistributions />
+ <SupportsParticleSizeDistributions>false</SupportsParticleSizeDistributions>
+ <ComponentDescription>Aquecedor</ComponentDescription>
+ <ComponentName>AQ-c01a6c84-aa27-4f9c-8c9c-4dee0b2a48f7</ComponentName>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <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>03/08/2025 17:25:25</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>AQ-c01a6c84-aa27-4f9c-8c9c-4dee0b2a48f7</Name>
+ <UserDefinedChartNames />
+ <ProductName>Heater</ProductName>
+ <ProductDescription>Simple heater model</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.8.3.0</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-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mole</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <TotalEnergyFlow>-5377.95368334893</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-21b9a837-83a5-46bf-a455-84eb5b4712ee</ComponentName>
+ <Name2>MAT-21b9a837-83a5-46bf-a455-84eb5b4712ee</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <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>03/08/2025 17:25:25</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-21b9a837-83a5-46bf-a455-84eb5b4712ee</Name>
+ <UserDefinedChartNames />
+ <ProductName>Material Stream</ProductName>
+ <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.8.3.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
+ <Phases>
+ <Phase>
+ <ID>0</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>9507.39614799116</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>1</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>2.01813194444444</MassFlow>
+ <MolarFlow>34.7222222222222</MolarFlow>
+ <Name>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.00730425485206246</VolumetricFlow>
+ <VolumetricFraction>2</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>Isobutene</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>Isobutene</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>Hydrogen</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>Hydrogen</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>552.590780392772</density>
+ <enthalpy>-342.297195915667</enthalpy>
+ <entropy>-1.31255662224538</entropy>
+ <heatCapacityCp>2.35663418087656</heatCapacityCp>
+ <heatCapacityCv>1.79749432684888</heatCapacityCv>
+ <massflow>2.01813194444444</massflow>
+ <molar_enthalpy>-19895.0660804496</molar_enthalpy>
+ <molar_entropy>-76.2886785094704</molar_entropy>
+ <molarflow>34.7222222222222</molarflow>
+ <molecularWeight>58.1222</molecularWeight>
+ <pressure>500000</pressure>
+ <surfaceTension>0.00985092396407804</surfaceTension>
+ <temperature>298.15</temperature>
+ <thermalConductivity>0.0947370488307205</thermalConductivity>
+ <volumetric_flow>0.00365212742603123</volumetric_flow>
+ <gibbs_free_energy>49.0415610067927</gibbs_free_energy>
+ <helmholtz_energy>48.1305714787113</helmholtz_energy>
+ <internal_energy>-343.208185443748</internal_energy>
+ <molar_gibbs_free_energy>2850.40341714901</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>2797.45470159996</molar_helmholtz_energy>
+ <molar_internal_energy>-19948.0147959986</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>9507.39614799116</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>2.01813194444444</MassFlow>
+ <MolarFlow>34.7222222222222</MolarFlow>
+ <Name>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000105436791510102</PartialVolume>
+ <VolumetricFlow>0.00365212742603123</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>Isobutene</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>Isobutene</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>9.53585915159453E-05</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>Hydrogen</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>Hydrogen</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>2.55002235074774E-05</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>0.0213604597241693</compressibilityFactor>
+ <density>552.590780392772</density>
+ <enthalpy>-342.297195915667</enthalpy>
+ <entropy>-1.31255662224538</entropy>
+ <heatCapacityCp>2.35663418087656</heatCapacityCp>
+ <heatCapacityCv>1.79749432684888</heatCapacityCv>
+ <kinematic_viscosity>2.97561274191656E-07</kinematic_viscosity>
+ <massflow>2.01813194444444</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>-19895.0660804496</molar_enthalpy>
+ <molar_entropy>-76.2886785094704</molar_entropy>
+ <molarflow>34.7222222222222</molarflow>
+ <molarfraction>1</molarfraction>
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+ <molar_internal_energy>-19948.0147959986</molar_internal_energy>
+ <volumetricFraction>1</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Isobutene</ComponentName>
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+ <Name>Isobutene</Name>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <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>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
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+ <idealGasHeatCapacityRatio>1.0921517375961</idealGasHeatCapacityRatio>
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+ <Phase>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <ComponentName>Isobutene</ComponentName>
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+ <lnKvalue>0</lnKvalue>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <lnKvalue>0</lnKvalue>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Liquid1</ComponentName>
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+ <Name>Liquid1</Name>
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+ <Properties>
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+ <Molarity>0</Molarity>
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+ <MolarFlow>0</MolarFlow>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <Molarity>0</Molarity>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
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+ <Name>Isobutene</Name>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <ComponentName>Isobutene</ComponentName>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
+ <molar_internal_energy>0</molar_internal_energy>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ReactorSizingType>Diameter</ReactorSizingType>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
+ <NumberOfTubes>12</NumberOfTubes>
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+ <dV>0.01</dV>
+ <CatalystLoading>1.2</CatalystLoading>
+ <CatalystVoidFraction>0.6</CatalystVoidFraction>
+ <CatalystParticleDiameter>0.1</CatalystParticleDiameter>
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+ <UserDefinedPressureDrop>0</UserDefinedPressureDrop>
+ <SlurryViscosityMode>0</SlurryViscosityMode>
+ <InternalSolver>0</InternalSolver>
+ <MobileCompatible>true</MobileCompatible>
+ <ObjectClass>Reactors</ObjectClass>
+ <OutletTemperature>873.149901748126</OutletTemperature>
+ <ReactorOperationMode>Isothermic</ReactorOperationMode>
+ <ReactionSetID>DefaultSet</ReactionSetID>
+ <ReactionSetName></ReactionSetName>
+ <DeltaP>62071.8981213107</DeltaP>
+ <DeltaT>0</DeltaT>
+ <DeltaQ>4257.22933546958</DeltaQ>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ParticleSizeDistributions />
+ <SupportsParticleSizeDistributions>false</SupportsParticleSizeDistributions>
+ <ComponentDescription>ReatorPFR</ComponentDescription>
+ <ComponentName>PFR-4d22f0c8-7656-4e51-a14f-6b03fe3c97d4</ComponentName>
+ <IsDirty>true</IsDirty>
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+ <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>03/08/2025 17:25:34</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>PFR-4d22f0c8-7656-4e51-a14f-6b03fe3c97d4</Name>
+ <UserDefinedChartNames />
+ <ProductName>Plug-Flow Reactor (PFR)</ProductName>
+ <ProductDescription>Plug-Flow Reactor model, supports Kinetic and HetCat reactions</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.8.3.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties>
+ <Property>
+ <Name>Max Sections</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>20.0</Data>
+ </Property>
+ <Property>
+ <Name>Reset Contents</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>0.0</Data>
+ </Property>
+ </DynamicProperties>
+ <DynamicPropertiesDescriptions>
+ <Property>
+ <Name>Max Sections</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Maximum number of sections to divide the PFR length in during dynamic calculations."</Data>
+ </Property>
+ <Property>
+ <Name>Reset Contents</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Empties the PFR's content on the next run."</Data>
+ </Property>
+ </DynamicPropertiesDescriptions>
+ <DynamicPropertiesUnitTypes>
+ <Property>
+ <Name>Max Sections</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>66</Data>
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+ <Property>
+ <Name>Reset Contents</Name>
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+ <Data>66</Data>
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+ </DynamicPropertiesUnitTypes>
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
+ <ReactionConversions />
+ <CompoundConversions>
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+ <Compound ID="Isobutene">0</Compound>
+ <Compound ID="Hydrogen">0</Compound>
+ </CompoundConversions>
+ <AccumulationStreams />
+ </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>2811.67554280151</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-30d381ad-56f9-4eef-b797-5d9159c1e9ca</ComponentName>
+ <Name2>MAT-30d381ad-56f9-4eef-b797-5d9159c1e9ca</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <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>03/08/2025 17:25:34</LastUpdated>
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+ <AdjustVarType>Manipulated</AdjustVarType>
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+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-30d381ad-56f9-4eef-b797-5d9159c1e9ca</Name>
+ <UserDefinedChartNames />
+ <ProductName>Material Stream</ProductName>
+ <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
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+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
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+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Isobutane</ComponentName>
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+ <PetroleumFraction>false</PetroleumFraction>
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+ <lnKvalue>NaN</lnKvalue>
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+ <MolarFlow>0.000725321332000038</MolarFlow>
+ <Name>Isobutane</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>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</ComponentName>
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+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>1.94809541600596</MassFlow>
+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Isobutene</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>
+ <Compound>
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+ <lnKvalue>NaN</lnKvalue>
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+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Hydrogen</Name>
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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>Mixture</ComponentName>
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+ <Name>Mixture</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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+ <heatCapacityCv>3.36839183503671</heatCapacityCv>
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+ <massfraction>1</massfraction>
+ <molar_enthalpy>49039.8713364966</molar_enthalpy>
+ <molar_entropy>123.024183576223</molar_entropy>
+ <molarflow>69.4437191233124</molarflow>
+ <molecularWeight>29.0614035355253</molecularWeight>
+ <pressure>237928.101878689</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>873.149901748126</temperature>
+ <thermalConductivity>0.263518547407596</thermalConductivity>
+ <volumetric_flow>2.11947205608175</volumetric_flow>
+ <gibbs_free_energy>-2008.80464683555</gibbs_free_energy>
+ <helmholtz_energy>-2258.68026308314</helmholtz_energy>
+ <internal_energy>1437.58147014362</internal_energy>
+ <molar_gibbs_free_energy>-58378.6824657262</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-65640.4185831854</molar_helmholtz_energy>
+ <molar_internal_energy>41778.1352190373</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</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>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>8.88395976096247E-05</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
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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>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</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>Isobutene</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>8.15793244523351E-05</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>Hydrogen</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>Hydrogen</Name>
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+ <PartialVolume>2.55002235074774E-05</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>OverallLiquid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>OverallLiquid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>0</density>
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+ <kinematic_viscosity>0</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>
+ <surfaceTension>NaN</surfaceTension>
+ <thermalConductivity>0</thermalConductivity>
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+ <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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>8.98735450626386E-05</ActivityCoeff>
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+ <MassFlow>4.21572715227726E-05</MassFlow>
+ <MolarFlow>0.000725321332000038</MolarFlow>
+ <Name>Isobutane</Name>
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+ <DiffusionCoefficient>9.57097225167953E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <DiffusionCoefficient>3.0088914821064E-09</DiffusionCoefficient>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
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+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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+ <molar_entropyF>-3.05595522024576</molar_entropyF>
+ <molarflow>69.4437191233124</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>29.0614035355253</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.263518547407596</thermalConductivity>
+ <viscosity>1.9432168483097E-05</viscosity>
+ <volumetric_flow>2.11947205608175</volumetric_flow>
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+ <idealGasHeatCapacityRatio>1.08493964710177</idealGasHeatCapacityRatio>
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+ </Properties>
+ </Phase>
+ <Phase>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ </Compound>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Isobutene</ComponentName>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ComponentName>Liquid1</ComponentName>
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+ <surfaceTension>NaN</surfaceTension>
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+ <lnKvalue>0</lnKvalue>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</Name>
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+ <ComponentName>Isobutene</ComponentName>
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+ <lnKvalue>0</lnKvalue>
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+ <Name>Isobutene</Name>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+ <surfaceTension>0</surfaceTension>
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+ <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>
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+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Double</PropertyType>
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+ </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>
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+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>46</Data>
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+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.Int64</PropertyType>
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+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>66</Data>
+ </Property>
+ </DynamicPropertiesUnitTypes>
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-197f7923-3f28-4292-a5c5-112562302b14</ComponentName>
+ <EnergyFlow>3152.94764717519</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-197f7923-3f28-4292-a5c5-112562302b14</Name2>
+ <code>0</code>
+ <IsDirty>false</IsDirty>
+ <CanUsePreviousResults>true</CanUsePreviousResults>
+ <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>03/08/2025 17:25:34</LastUpdated>
+ <ErrorMessage></ErrorMessage>
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+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-197f7923-3f28-4292-a5c5-112562302b14</Name>
+ <UserDefinedChartNames />
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.8.3.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.ComponentSeparator</Type>
+ <EmbeddedImageData></EmbeddedImageData>
+ <UseEmbeddedImage>false</UseEmbeddedImage>
+ <ObjectClass>Separators</ObjectClass>
+ <SpecifiedStreamIndex>0</SpecifiedStreamIndex>
+ <EnergyImb>4.59285239396169</EnergyImb>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ParticleSizeDistributions />
+ <SupportsParticleSizeDistributions>false</SupportsParticleSizeDistributions>
+ <ComponentDescription>ComponentSeparator</ComponentDescription>
+ <ComponentName>CS-f60f2021-769c-4ac2-a94e-d16282289f59</ComponentName>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <SupportsDynamicMode>false</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>03/08/2025 17:25:34</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>CS-f60f2021-769c-4ac2-a94e-d16282289f59</Name>
+ <UserDefinedChartNames />
+ <ProductName>Compound Separator</ProductName>
+ <ProductDescription>Model for a hypothetical compound separation process</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.8.3.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
+ <SeparationSpecs>
+ <SeparationSpec ID="Isobutane" CompID="Isobutane" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="0" />
+ <SeparationSpec ID="Isobutene" CompID="Isobutene" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="0" />
+ <SeparationSpec ID="Hydrogen" CompID="Hydrogen" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="100" />
+ </SeparationSpecs>
+ </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>-341.272104373685</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-40f14f63-807d-4fa6-9531-62f99f9e0a17</ComponentName>
+ <Name2>MAT-40f14f63-807d-4fa6-9531-62f99f9e0a17</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <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>03/08/2025 17:25:34</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-40f14f63-807d-4fa6-9531-62f99f9e0a17</Name>
+ <UserDefinedChartNames />
+ <ProductName>Material Stream</ProductName>
+ <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.8.3.0</ProductVersion>
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+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
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+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
+ <Phases>
+ <Phase>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
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+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>4.21572715227726E-05</MassFlow>
+ <MolarFlow>0.000725321332000038</MolarFlow>
+ <Name>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>8.82348059635765E-06</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
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+ <MassFraction>0.965296358032047</MassFraction>
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+ <Molarity>40.335621737539</Molarity>
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+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>1.94809541600596</MassFlow>
+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Isobutene</Name>
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+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.422496271735869</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>
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+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.0699943711727681</MassFlow>
+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Hydrogen</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>Mixture</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Mixture</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>2.34444404744163</density>
+ <enthalpy>125.147121551883</enthalpy>
+ <entropy>1.62183187537417</entropy>
+ <heatCapacityCp>2.26324118232534</heatCapacityCp>
+ <heatCapacityCv>1.96231643778977</heatCapacityCv>
+ <massflow>2.01813194445026</massflow>
+ <molar_enthalpy>3636.9510007287</molar_enthalpy>
+ <molar_entropy>47.1327105970264</molar_entropy>
+ <molarflow>69.4437191233124</molarflow>
+ <molecularWeight>29.0614035355253</molecularWeight>
+ <pressure>237928.101878689</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>358.15</temperature>
+ <thermalConductivity>0.114012210170694</thermalConductivity>
+ <volumetric_flow>0.860814719230572</volumetric_flow>
+ <gibbs_free_energy>-455.711964613375</gibbs_free_energy>
+ <helmholtz_energy>-557.197902031386</helmholtz_energy>
+ <internal_energy>23.6611841338723</internal_energy>
+ <molar_gibbs_free_energy>-13243.6292995963</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-16192.9530800822</molar_helmholtz_energy>
+ <molar_internal_energy>687.627220242831</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</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>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000128786315555585</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>Isobutene</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>Isobutene</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000113772032665325</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>Hydrogen</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>Hydrogen</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>2.55002235074774E-05</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>0</density>
+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>0</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>
+ <surfaceTension>NaN</surfaceTension>
+ <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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0.155612511312472</ActivityCoeff>
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+ <MoleFraction>1.04447362721468E-05</MoleFraction>
+ <Molarity>0.000842598663564161</Molarity>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>4.21572715227726E-05</MassFlow>
+ <MolarFlow>0.000725321332000038</MolarFlow>
+ <Name>Isobutane</Name>
+ <PartialPressure>2.48509627585539</PartialPressure>
+ <PartialVolume>12.1649258968888</PartialVolume>
+ <VolumetricFlow>8.82348059635765E-06</VolumetricFlow>
+ <VolumetricFraction>1.02501506993798E-05</VolumetricFraction>
+ <DiffusionCoefficient>2.01216834578013E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</ComponentName>
+ <ActivityCoeff>0.168662236495354</ActivityCoeff>
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+ <Molarity>40.335621737539</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.972735265577351</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>1.94809541600596</MassFlow>
+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Isobutene</Name>
+ <PartialPressure>118962.808391207</PartialPressure>
+ <PartialVolume>12.1681463390116</PartialVolume>
+ <VolumetricFlow>0.422496271735869</VolumetricFlow>
+ <VolumetricFraction>0.490809766953697</VolumetricFraction>
+ <DiffusionCoefficient>2.1241439386003E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
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+ <PetroleumFraction>false</PetroleumFraction>
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+ <lnKvalue>0</lnKvalue>
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+ <Name>Hydrogen</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.990484028371775</compressibilityFactor>
+ <density>2.34444404744163</density>
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+ <enthalpyF>-169.102969363407</enthalpyF>
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+ <entropyF>1.62160437243077</entropyF>
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+ <heatCapacityCv>1.96231643778977</heatCapacityCv>
+ <jouleThomsonCoefficient>5.62653101213118E-06</jouleThomsonCoefficient>
+ <kinematic_viscosity>4.33576328176409E-06</kinematic_viscosity>
+ <massflow>2.01813194445026</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>3636.9510007287</molar_enthalpy>
+ <molar_enthalpyF>-4914.36963172555</molar_enthalpyF>
+ <molar_entropy>47.1327105970264</molar_entropy>
+ <molar_entropyF>-78.9474281994426</molar_entropyF>
+ <molarflow>69.4437191233124</molarflow>
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+ <viscosity>1.01649544170478E-05</viscosity>
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+ <helmholtz_energy>-557.197902031386</helmholtz_energy>
+ <internal_energy>23.6611841338723</internal_energy>
+ <isothermal_compressibility>4.24329720090836E-06</isothermal_compressibility>
+ <molar_gibbs_free_energy>-13243.6292995963</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-16192.9530800822</molar_helmholtz_energy>
+ <molar_internal_energy>687.627220242831</molar_internal_energy>
+ <idealGasHeatCapacityCp>2.25065054527132</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.1456218927348</idealGasHeatCapacityRatio>
+ <volumetricFraction>1</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
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+ <MassFraction>2.03777534725211E-05</MassFraction>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</ComponentName>
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+ <PetroleumFraction>false</PetroleumFraction>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</Name>
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+ <VolumetricFlow>0</VolumetricFlow>
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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>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Hydrogen</ComponentName>
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+ <lnKvalue>0</lnKvalue>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</Name>
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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>Liquid1</ComponentName>
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+ <Name>Liquid1</Name>
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <surfaceTension>0.0048541748197096</surfaceTension>
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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>
+ <idealGasHeatCapacityCp>1.69530338074953</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.09215173759638</idealGasHeatCapacityRatio>
+ <volumetricFraction>0</volumetricFraction>
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
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+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</Name>
+ <PartialPressure>NaN</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</Name>
+ <PartialPressure>NaN</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>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
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+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</Name>
+ <PartialPressure>NaN</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>
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+ <Name>Liquid2</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <surfaceTension>0</surfaceTension>
+ <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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</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>
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+ <ComponentName>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <Molarity>0</Molarity>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</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>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</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>
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+ <ComponentName>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</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>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>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</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>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</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>Solid</ComponentName>
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+ <molar_internal_energy>0</molar_internal_energy>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
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+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
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+ <DynamicsSpec>Pressure</DynamicsSpec>
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+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
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+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
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+ <AdjustVarType>Manipulated</AdjustVarType>
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+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-8b8abedd-b555-4da8-8283-4d56d7a8f221</Name>
+ <UserDefinedChartNames />
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
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+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mass</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <TotalEnergyFlow>60.2081703648204</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
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+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
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+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-1042f315-8a0f-4362-bc09-3132f33c0a16</Name>
+ <UserDefinedChartNames />
+ <ProductName>Material Stream</ProductName>
+ <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+ <ProductAuthor>Daniel Wagner</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
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+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
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+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-cb481779-6616-4ab7-b966-bf6af4f09801</PropertyPackage>
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+ <Compounds>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
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+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</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>Isobutene</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>
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+ <ComponentName>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>1</MassFraction>
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+ <Molarity>79.8494176196147</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.0699943711727681</MassFlow>
+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Hydrogen</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>Mixture</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Mixture</Name>
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>0.160966843991029</density>
+ <enthalpy>860.185888608209</enthalpy>
+ <entropy>-0.895361637193638</entropy>
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+ <heatCapacityCv>10.2894636340011</heatCapacityCv>
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+ <molar_entropy>-1.80494161718591</molar_entropy>
+ <molarflow>34.7214969009902</molarflow>
+ <molecularWeight>2.01588</molecularWeight>
+ <pressure>237928.101878689</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>358.150000038686</temperature>
+ <thermalConductivity>0.205397935570816</thermalConductivity>
+ <volumetric_flow>0.434837196514017</volumetric_flow>
+ <gibbs_free_energy>1180.85965900375</gibbs_free_energy>
+ <helmholtz_energy>-297.259039104973</helmholtz_energy>
+ <internal_energy>-617.932809500513</internal_energy>
+ <molar_gibbs_free_energy>2380.47136939248</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-599.238551750933</molar_helmholtz_energy>
+ <molar_internal_energy>-1245.67839201589</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Compounds>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</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>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000128786315581541</PartialVolume>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</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>Isobutene</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000113772032683781</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Hydrogen</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>Hydrogen</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>2.55002235074774E-05</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>0</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>OverallLiquid</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>OverallLiquid</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>0</density>
+ <enthalpy>0</enthalpy>
+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>0</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>
+ <surfaceTension>NaN</surfaceTension>
+ <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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>1</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>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>2.01216834616049E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</ComponentName>
+ <ActivityCoeff>1</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>Isobutene</Name>
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+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>2.12414393900182E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Hydrogen</ComponentName>
+ <ActivityCoeff>2.87618234571604E-21</ActivityCoeff>
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+ <Name>Hydrogen</Name>
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+ <DiffusionCoefficient>6.32579014766653E-10</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>1.00068873593406</compressibilityFactor>
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+ <heatCapacityCp>14.4238827535983</heatCapacityCp>
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+ <kinematic_viscosity>6.30306469030633E-05</kinematic_viscosity>
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+ <molar_entropyF>-1.80494161718591</molar_entropyF>
+ <molarflow>34.7214969009902</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>2.01588</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.205397935570816</thermalConductivity>
+ <viscosity>1.0145844306699E-05</viscosity>
+ <volumetric_flow>0.434837196514017</volumetric_flow>
+ <bulk_modulus>-463662864.201858</bulk_modulus>
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+ <internal_energy>-617.932809500513</internal_energy>
+ <isothermal_compressibility>-2.15673947000562E-09</isothermal_compressibility>
+ <molar_gibbs_free_energy>2380.47136939248</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-599.238551750933</molar_helmholtz_energy>
+ <molar_internal_energy>-1245.67839201589</molar_internal_energy>
+ <idealGasHeatCapacityCp>14.4181451417923</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.40065055494714</idealGasHeatCapacityRatio>
+ <volumetricFraction>1</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
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+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
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+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
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+ <lnKvalue>0</lnKvalue>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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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+ <ComponentName>Isobutene</ComponentName>
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+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
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+ <VolumetricFraction>0.999976340897553</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>Hydrogen</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>Hydrogen</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>4.65177736083779</density>
+ <enthalpy>96.3804525802489</enthalpy>
+ <entropy>0.17417137592053</entropy>
+ <heatCapacityCp>1.83671175738969</heatCapacityCp>
+ <heatCapacityCv>1.66271920076283</heatCapacityCv>
+ <massflow>1.94813757327749</massflow>
+ <molar_enthalpy>5407.5565728153</molar_enthalpy>
+ <molar_entropy>9.77212228663427</molar_entropy>
+ <molarflow>34.7222222223222</molarflow>
+ <molecularWeight>56.1063621102301</molecularWeight>
+ <pressure>237928.101878689</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>358.15</temperature>
+ <thermalConductivity>0.0226283937675163</thermalConductivity>
+ <volumetric_flow>0.418794241890937</volumetric_flow>
+ <gibbs_free_energy>34.000974294311</gibbs_free_energy>
+ <helmholtz_energy>-17.1468093209903</helmholtz_energy>
+ <internal_energy>45.2326689649475</internal_energy>
+ <molar_gibbs_free_energy>1907.67097585724</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-962.045092798552</molar_helmholtz_energy>
+ <molar_internal_energy>2537.84050415951</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</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>Isobutane</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000128786315555585</PartialVolume>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</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>Isobutene</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.000113772032665325</PartialVolume>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Hydrogen</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>Hydrogen</Name>
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+ <PartialVolume>2.55002235074774E-05</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
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+ <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>0</density>
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+ <entropy>0</entropy>
+ <heatCapacityCp>0</heatCapacityCp>
+ <heatCapacityCv>0</heatCapacityCv>
+ <kinematic_viscosity>0</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>
+ <surfaceTension>NaN</surfaceTension>
+ <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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>2</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0.154263246609693</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>2.16397815539528E-05</MassFraction>
+ <MoleFraction>2.0889254361541E-05</MoleFraction>
+ <Molarity>0.00173192766148138</Molarity>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>4.21572715227726E-05</MassFlow>
+ <MolarFlow>0.000725321332000038</MolarFlow>
+ <Name>Isobutane</Name>
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+ <PartialVolume>0.12937399599132</PartialVolume>
+ <VolumetricFlow>9.90829587320997E-06</VolumetricFlow>
+ <VolumetricFraction>2.36591024472354E-05</VolumetricFraction>
+ <DiffusionCoefficient>2.01216834578013E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutene</ComponentName>
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+ <Molarity>82.9082480795723</Molarity>
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+ <FugacityCoeff>0.964807845360006</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>1.94809541600596</MassFlow>
+ <MolarFlow>34.7214969009902</MolarFlow>
+ <Name>Isobutene</Name>
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+ <VolumetricFraction>0.999976340897553</VolumetricFraction>
+ <DiffusionCoefficient>2.1241439386003E-11</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Hydrogen</ComponentName>
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+ <Molarity>0</Molarity>
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+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</Name>
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+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.963749029785106</compressibilityFactor>
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+ <enthalpyF>-208.441710022204</enthalpyF>
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+ <heatCapacityCp>1.83671175738969</heatCapacityCp>
+ <heatCapacityCv>1.66271920076283</heatCapacityCv>
+ <jouleThomsonCoefficient>1.34478722430892E-06</jouleThomsonCoefficient>
+ <kinematic_viscosity>2.18858479614202E-06</kinematic_viscosity>
+ <massflow>1.94813757327749</massflow>
+ <massfraction>1</massfraction>
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+ <molar_enthalpyF>-11694.9060613814</molar_enthalpyF>
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+ <molar_entropyF>-242.385521586215</molar_entropyF>
+ <molarflow>34.7222222223222</molarflow>
+ <molarfraction>1</molarfraction>
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+ <volumetric_flow>0.418794241890937</volumetric_flow>
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+ <helmholtz_energy>-17.1468093209903</helmholtz_energy>
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+ <isothermal_compressibility>2.17992572547101E-08</isothermal_compressibility>
+ <molar_gibbs_free_energy>1907.67097585724</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-962.045092798552</molar_helmholtz_energy>
+ <molar_internal_energy>2537.84050415951</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.81348627889321</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.08898248511049</idealGasHeatCapacityRatio>
+ <volumetricFraction>1</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
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+ <MassFraction>2.02728132552711E-05</MassFraction>
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+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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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+ <ComponentName>Isobutene</ComponentName>
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+ <FugacityCoeff>4.38761555874891</FugacityCoeff>
+ <Kvalue>0</Kvalue>
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+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</Name>
+ <PartialPressure>1043916.61213665</PartialPressure>
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+ <VolumetricFlow>0</VolumetricFlow>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
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+ <ComponentName>Hydrogen</ComponentName>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ComponentName>Liquid1</ComponentName>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
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+ <Molarity>0</Molarity>
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+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</Name>
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+ <VolumetricFlow>0</VolumetricFlow>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Isobutene</ComponentName>
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+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
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+ <FugacityCoeff>NaN</FugacityCoeff>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</Name>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
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+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
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+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</Name>
+ <PartialPressure>NaN</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>
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+ <Name>Liquid2</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <surfaceTension>0</surfaceTension>
+ <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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>5</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <Molarity>0</Molarity>
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+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</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>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</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>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</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>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</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>Isobutane</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutane</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>Isobutene</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Isobutene</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>Hydrogen</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>NaN</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Hydrogen</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>
+ <volumetricFraction>0</volumetricFraction>
+ </Properties>
+ </Phase>
+ </Phases>
+ </SimulationObject>
+ </SimulationObjects>
+ <Settings>
+ <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables</Type>
+ <SimulationMode></SimulationMode>
+ <BackupFileName>59890291.dwbcs</BackupFileName>
+ <FilePath>C:\Users\aruls\OneDrive\Desktop\Recent_works\flowsheeting\submision\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>D1EE95D263991CD59AD62F52E096975ABD89A397</Key>
+ <NumberFormat>G6</NumberFormat>
+ <Password></Password>
+ <SimulationAuthor>SAISIDHARTH_NB\aruls</SimulationAuthor>
+ <SimulationComments></SimulationComments>
+ <SimulationName>MySimulation_35</SimulationName>
+ <UsePassword>false</UsePassword>
+ <SelectedUnitSystem1>
+ <Type>DWSIM.SharedClasses.SystemsOfUnits.SI_ENG</Type>
+ <accel>m2/s</accel>
+ <activity>Pa</activity>
+ <activityCoefficient>-</activityCoefficient>
+ <area>m2</area>
+ <cakeresistance>m/kg</cakeresistance>
+ <cinematic_viscosity>cSt</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>
+ <heat>kJ</heat>
+ <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>mol/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>SI (Engineering)</Name>
+ <pdp_boilingPointTemperature>C</pdp_boilingPointTemperature>
+ <pdp_meltingTemperature>C</pdp_meltingTemperature>
+ <pressure>bar</pressure>
+ <reac_rate>mol/[m3.s]</reac_rate>
+ <reac_rate_heterog>mol/[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>s</time>
+ <vaporPressure>bar</vaporPressure>
+ <velocity>m/s</velocity>
+ <viscosity>cP</viscosity>
+ <viscosityOfLiquid>cP</viscosityOfLiquid>
+ <viscosityOfVapor>cP</viscosityOfVapor>
+ <volume>m3</volume>
+ <volumetricFlow>m3/h</volumetricFlow>
+ <diffusivity>m2/s</diffusivity>
+ <conductance>[kg/s]/[Pa^0.5]</conductance>
+ <mole>kmol</mole>
+ <emission_factor>[kg/s]/kW</emission_factor>
+ <specific_power>kW/[ton/h]</specific_power>
+ </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>
+ <CustomCalculationOrder />
+ <SpecCalculationMode>AfterSourceObject</SpecCalculationMode>
+ <ForceObjectSolving>true</ForceObjectSolving>
+ <SaveFlowsheetMessagesInFile>true</SaveFlowsheetMessagesInFile>
+ <RTFAnnotations></RTFAnnotations>
+ <EnabledUndoRedo>true</EnabledUndoRedo>
+ <EnableGHGEmissionsSubsystem>false</EnableGHGEmissionsSubsystem>
+ <FlowsheetTransitionObject>
+ <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetTransitionRestore</Type>
+ <FeatureName></FeatureName>
+ <FeatureType></FeatureType>
+ <Action></Action>
+ <Location></Location>
+ <Position />
+ </FlowsheetTransitionObject>
+ <UniqueID>c101119b-444f-4de0-8d83-b13c6f989585</UniqueID>
+ <VisibleProperties>
+ <ObjectType Value="AbsorptionColumn">
+ <PropertyID Value="PROP_AC_0" />
+ <PropertyID Value="PROP_AC_1" />
+ <PropertyID Value="PROP_AC_2" />
+ <PropertyID Value="Estimated Height" />
+ <PropertyID Value="Estimated Diameter" />
+ <PropertyID Value="Number of Stages" />
+ </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">
+ <PropertyID Value="Monitored Value" />
+ </ObjectType>
+ <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" />
+ <PropertyID Value="PressureRatio" />
+ </ObjectType>
+ <ObjectType Value="Cooler">
+ <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">
+ <PropertyID Value="Monitored Value" />
+ </ObjectType>
+ <ObjectType Value="DistillationColumn">
+ <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" />
+ <PropertyID Value="Estimated Height" />
+ <PropertyID Value="Estimated Diameter" />
+ </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" />
+ <PropertyID Value="PressureRatio" />
+ </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="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" />
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+ <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">
+ <PropertyID Value="Monitored Value" />
+ </ObjectType>
+ <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="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" />
+ <PropertyID Value="PROP_PU_6" />
+ </ObjectType>
+ <ObjectType Value="PythonController">
+ <PropertyID Value="Active" />
+ <PropertyID Value="SetPoint" />
+ <PropertyID Value="Output" />
+ </ObjectType>
+ <ObjectType Value="Reactor_Conversion">
+ <PropertyID Value="PROP_CR_0" />
+ <PropertyID Value="Calculation Mode" />
+ </ObjectType>
+ <ObjectType Value="Reactor_CSTR">
+ <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="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="PROP_PF_10" />
+ <PropertyID Value="Calculation Mode" />
+ </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="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" />
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+ <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="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" />
+ <PropertyID Value="PROP_VA_6" />
+ <PropertyID Value="Actual Flow Coefficient" />
+ </ObjectType>
+ <ObjectType Value="Vessel">
+ <PropertyID Value="PROP_SV_0" />
+ <PropertyID Value="PROP_SV_1" />
+ </ObjectType>
+ <ObjectType Value="NeuralNetworkUnitOperation">
+ <PropertyID Value="Status" />
+ <PropertyID Value="Status" />
+ </ObjectType>
+ <ObjectType Value="PipeNetworkUnitOperation">
+ <PropertyID Value="Status" />
+ <PropertyID Value="Number of Network Objects" />
+ <PropertyID Value="Mass Balance Residual" />
+ <PropertyID Value="Pressure Balance Residual" />
+ <PropertyID Value="Energy Balance Residual" />
+ </ObjectType>
+ <ObjectType Value="HydroelectricTurbine">
+ <PropertyID Value="Efficiency" />
+ <PropertyID Value="Static Head" />
+ <PropertyID Value="Velocity Head" />
+ <PropertyID Value="Total Head" />
+ <PropertyID Value="Inlet Velocity" />
+ <PropertyID Value="Outlet Velocity" />
+ <PropertyID Value="Generated Power" />
+ </ObjectType>
+ <ObjectType Value="PEMFC_Amphlett">
+ <PropertyID Value="i-start" />
+ <PropertyID Value="i-stop" />
+ <PropertyID Value="i-step" />
+ <PropertyID Value="A" />
+ <PropertyID Value="l" />
+ <PropertyID Value="lambda" />
+ <PropertyID Value="R" />
+ <PropertyID Value="JMax" />
+ <PropertyID Value="N" />
+ </ObjectType>
+ <ObjectType Value="SolarPanel">
+ <PropertyID Value="Efficiency" />
+ <PropertyID Value="User-Defined Solar Irradiation" />
+ <PropertyID Value="Actual Solar Irradiation" />
+ <PropertyID Value="Panel Area" />
+ <PropertyID Value="Number of Panels" />
+ <PropertyID Value="Generated Power" />
+ </ObjectType>
+ <ObjectType Value="WaterElectrolyzer">
+ <PropertyID Value="Voltage" />
+ <PropertyID Value="Thermoneutral Voltage" />
+ <PropertyID Value="Reversible Voltage" />
+ <PropertyID Value="Number of Cells" />
+ <PropertyID Value="Cell Voltage" />
+ <PropertyID Value="Waste Heat" />
+ <PropertyID Value="Current" />
+ <PropertyID Value="Electron Transfer" />
+ <PropertyID Value="Efficiency" />
+ <PropertyID Value="Input Efficiency" />
+ </ObjectType>
+ <ObjectType Value="WindTurbine">
+ <PropertyID Value="Efficiency" />
+ <PropertyID Value="User-Defined Wind Speed" />
+ <PropertyID Value="Actual Wind Speed" />
+ <PropertyID Value="User-Defined Air Temperature" />
+ <PropertyID Value="Actual Air Temperature" />
+ <PropertyID Value="User-Defined Air Pressure" />
+ <PropertyID Value="Actual Air Pressure" />
+ <PropertyID Value="User-Defined Relative Humidity" />
+ <PropertyID Value="Actual Relative Humidity" />
+ <PropertyID Value="Disk Area" />
+ <PropertyID Value="Rotor Diameter" />
+ <PropertyID Value="Number of Units" />
+ <PropertyID Value="Generated Power" />
+ <PropertyID Value="Maximum Theoretical Power" />
+ <PropertyID Value="Calculated Air Density" />
+ </ObjectType>
+ <ObjectType Value="Reactor_ReaktoroGibbs" />
+ </VisibleProperties>
+ </Settings>
+ <DynamicProperties />
+ <GraphicObjects>
+ <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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+ <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-c01a6c84-aa27-4f9c-8c9c-4dee0b2a48f7</Name>
+ <Tag>HT-01</Tag>
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+ <Rotation>0</Rotation>
+ <DrawMode>0</DrawMode>
+ <DrawLabel>true</DrawLabel>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-21b9a837-83a5-46bf-a455-84eb5b4712ee" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-811a7074-ae10-41e1-ac6c-cfead4850090" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-f70fa01e-f02f-4853-8ec8-ba79f9bac2cd" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
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+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
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+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
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+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
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+ <DrawLabel>true</DrawLabel>
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+ </OutputConnectors>
+ <EnergyConnector>
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+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Fill>true</Fill>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
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+ <FlippedV>false</FlippedV>
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+ <ObjectType>MaterialStream</ObjectType>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-f70fa01e-f02f-4853-8ec8-ba79f9bac2cd</Name>
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+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="PFR-4d22f0c8-7656-4e51-a14f-6b03fe3c97d4" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
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+ <SpecialConnectors />
+ </GraphicObject>
+ <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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+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
+ <FlippedH>false</FlippedH>
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+ <ObjectType>EnergyStream</ObjectType>
+ <Shape>0</Shape>
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+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>EN-811a7074-ae10-41e1-ac6c-cfead4850090</Name>
+ <Tag>E-01</Tag>
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+ <DrawMode>0</DrawMode>
+ <DrawLabel>true</DrawLabel>
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+ <Connector IsAttached="false" />
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+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="AQ-c01a6c84-aa27-4f9c-8c9c-4dee0b2a48f7" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
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+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.PFRGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <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>PFR</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>RCT_PFR</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>PFR-4d22f0c8-7656-4e51-a14f-6b03fe3c97d4</Name>
+ <Tag>R-01</Tag>
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+ <Selected>false</Selected>
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+ <DrawMode>0</DrawMode>
+ <DrawLabel>true</DrawLabel>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-f70fa01e-f02f-4853-8ec8-ba79f9bac2cd" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-de540dd1-9e7e-44d4-8fce-b87abf4acb53" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-30d381ad-56f9-4eef-b797-5d9159c1e9ca" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <FillColor>#ffffffff</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>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-30d381ad-56f9-4eef-b797-5d9159c1e9ca</Name>
+ <Tag>S-03</Tag>
+ <Width>20</Width>
+ <X>1061.082</X>
+ <Y>403.7898</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>0</DrawMode>
+ <DrawLabel>true</DrawLabel>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="PFR-4d22f0c8-7656-4e51-a14f-6b03fe3c97d4" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="RESF-882b3589-ef4e-4e9e-b460-b4b62c688424" 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>
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+ <DrawMode>0</DrawMode>
+ <DrawLabel>true</DrawLabel>
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+ <Connector IsAttached="false" />
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+ </OutputConnectors>
+ <EnergyConnector>
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+ </GraphicObject>
+ <GraphicObject>
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+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
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+ <Active>true</Active>
+ <Description>Material Stream Cooler</Description>
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+ <IsEnergyStream>false</IsEnergyStream>
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+ <Status>Calculated</Status>
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+ </OutputConnectors>
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+ <ObjectType>EnergyStream</ObjectType>
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+ </InputConnectors>
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+ <GraphicObject>
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+ <GradientMode>true</GradientMode>
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+ <Active>true</Active>
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+ </OutputConnectors>
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+ </InputConnectors>
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+ <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Hydrogen>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Hydrogen>
+ <Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Hydrogen>false</Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Hydrogen>
+ <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Hydrogen>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Hydrogen>
+ <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Hydrogen>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Hydrogen>
+ <Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Hydrogen>false</Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Hydrogen>
+ <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Hydrogen>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Hydrogen>
+ <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Hydrogen>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Hydrogen>
+ <PROP_MS_250>false</PROP_MS_250>
+ <PROP_MS_251>false</PROP_MS_251>
+ <PROP_MS_252>false</PROP_MS_252>
+ <PROP_MS_253>false</PROP_MS_253>
+ <PROP_MS_254>false</PROP_MS_254>
+ <PROP_MS_255>false</PROP_MS_255>
+ <PROP_MS_256>false</PROP_MS_256>
+ <PROP_MS_257>false</PROP_MS_257>
+ <PROP_MS_258>false</PROP_MS_258>
+ <PROP_MS_259>false</PROP_MS_259>
+ <CO2_x0020_Loading>false</CO2_x0020_Loading>
+ <CO2_x0020_Partial_x0020_Pressure>false</CO2_x0020_Partial_x0020_Pressure>
+ <H2S_x0020_Loading>false</H2S_x0020_Loading>
+ <H2S_x0020_Partial_x0020_Pressure>false</H2S_x0020_Partial_x0020_Pressure>
+ <Mean_x0020_Particle_x0020_Size_x0020__x0028_Solid_x0029_>false</Mean_x0020_Particle_x0020_Size_x0020__x0028_Solid_x0029_>
+ <Particle_x0020_Size_x0020_Standard_x0020_Deviation_x0020__x0028_Solid_x0029_>false</Particle_x0020_Size_x0020_Standard_x0020_Deviation_x0020__x0028_Solid_x0029_>
+ <PROP_MS_260>false</PROP_MS_260>
+ <PROP_MS_261>false</PROP_MS_261>
+ <PROP_MS_262>false</PROP_MS_262>
+ <PROP_MS_263>false</PROP_MS_263>
+ <PROP_MS_264>false</PROP_MS_264>
+ </Properties>
+ <SortableItems>
+ <SortableItem>Name | ASC</SortableItem>
+ <SortableItem>Name | DESC</SortableItem>
+ <SortableItem>Temperature | ASC</SortableItem>
+ <SortableItem>Temperature | DESC</SortableItem>
+ <SortableItem>Pressure | ASC</SortableItem>
+ <SortableItem>Pressure | DESC</SortableItem>
+ <SortableItem>Mass Flow | ASC</SortableItem>
+ <SortableItem>Mass Flow | DESC</SortableItem>
+ <SortableItem>Molar Flow | ASC</SortableItem>
+ <SortableItem>Molar Flow | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Isobutane | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Isobutane | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Isobutene | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Isobutene | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Hydrogen | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Mixture) / Hydrogen | DESC</SortableItem>
+ <SortableItem>Custom</SortableItem>
+ </SortableItems>
+ </GraphicObject>
+ </GraphicObjects>
+ <PropertyPackages>
+ <PropertyPackage>
+ <ID>PP-cb481779-6616-4ab7-b966-bf6af4f09801</ID>
+ <Type>DWSIM.Thermodynamics.PropertyPackages.PengRobinsonPropertyPackage</Type>
+ <ComponentName>Peng-Robinson (PR)</ComponentName>
+ <ComponentDescription>Property Package that uses the Peng-Robinson Cubic Equation of State. Recommended for use with hydrocarbons and non-condensables.</ComponentDescription>
+ <Tag>Peng-Robinson (PR) (1)</Tag>
+ <UseHenryConstants>true</UseHenryConstants>
+ <AutoEstimateMissingNRTLUNIQUACParameters>true</AutoEstimateMissingNRTLUNIQUACParameters>
+ <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>
+ <LiquidEnthalpyEntropyCpCvCalculationMode_EOS>EOS</LiquidEnthalpyEntropyCpCvCalculationMode_EOS>
+ <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
+ <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
+ <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
+ <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
+ <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
+ <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
+ <DisplayMissingCompoundPropertiesWarning>false</DisplayMissingCompoundPropertiesWarning>
+ <ForcedSolids>[]</ForcedSolids>
+ <PropertyOverrides>{}</PropertyOverrides>
+ <InteractionParameters />
+ <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="False" />
+ <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
+ <Setting Name="FailSafeCalculationMode" Value="1" />
+ </FlashSettings>
+ </PropertyPackage>
+ </PropertyPackages>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+ <Acentric_Factor>0.186</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>75-28-5</CAS_Number>
+ <Chao_Seader_Acentricity>0.1825</Chao_Seader_Acentricity>
+ <Chao_Seader_Liquid_Molar_Volume>105.5</Chao_Seader_Liquid_Molar_Volume>
+ <Chao_Seader_Solubility_Parameter>0.00328800419366</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <Critical_Compressibility>0.278</Critical_Compressibility>
+ <Critical_Pressure>3640000</Critical_Pressure>
+ <Critical_Temperature>407.85</Critical_Temperature>
+ <Critical_Volume>0.2627</Critical_Volume>
+ <CurrentDB>ChemSep</CurrentDB>
+ <Dipole_Moment>4.4E-31</Dipole_Moment>
+ <Electrolyte_Cp0>0</Electrolyte_Cp0>
+ <Electrolyte_DelGF>0</Electrolyte_DelGF>
+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
+ <EnthalpyOfFusionAtTf>4.54</EnthalpyOfFusionAtTf>
+ <Formula>CH3CH(CH3)CH3</Formula>
+ <HVap_A>34869000</HVap_A>
+ <HVap_B>0.64449</HVap_B>
+ <HVap_C>-0.15424</HVap_C>
+ <HVap_D>-0.28822</HVap_D>
+ <HVap_E>0.20982</HVap_E>
+ <HVap_TMAX>407.8</HVap_TMAX>
+ <HVap_TMIN>113.54</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>4</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>39746.03</Ideal_Gas_Heat_Capacity_Const_A>
+ <Ideal_Gas_Heat_Capacity_Const_B>-371.573</Ideal_Gas_Heat_Capacity_Const_B>
+ <Ideal_Gas_Heat_Capacity_Const_C>12.02593</Ideal_Gas_Heat_Capacity_Const_C>
+ <Ideal_Gas_Heat_Capacity_Const_D>0.000755039</Ideal_Gas_Heat_Capacity_Const_D>
+ <Ideal_Gas_Heat_Capacity_Const_E>-2.59608E-07</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>16</IdealgasCpEquation>
+ <IG_Enthalpy_of_Formation_25C>-2322.52048270712</IG_Enthalpy_of_Formation_25C>
+ <IG_Entropy_of_Formation_25C>-6.55254904594069</IG_Entropy_of_Formation_25C>
+ <IG_Gibbs_Energy_of_Formation_25C>-368.877984659906</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>0.89934</Liquid_Density_Const_A>
+ <Liquid_Density_Const_B>0.25371</Liquid_Density_Const_B>
+ <Liquid_Density_Const_C>407.85</Liquid_Density_Const_C>
+ <Liquid_Density_Const_D>0.25125</Liquid_Density_Const_D>
+ <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+ <Liquid_Density_Tmax>407.84</Liquid_Density_Tmax>
+ <Liquid_Density_Tmin>113.54</Liquid_Density_Tmin>
+ <Liquid_Heat_Capacity_Const_A>89466</Liquid_Heat_Capacity_Const_A>
+ <Liquid_Heat_Capacity_Const_B>-323.61</Liquid_Heat_Capacity_Const_B>
+ <Liquid_Heat_Capacity_Const_C>12.827</Liquid_Heat_Capacity_Const_C>
+ <Liquid_Heat_Capacity_Const_D>-0.010476</Liquid_Heat_Capacity_Const_D>
+ <Liquid_Heat_Capacity_Const_E>2.5037E-05</Liquid_Heat_Capacity_Const_E>
+ <Liquid_Heat_Capacity_Tmax>380</Liquid_Heat_Capacity_Tmax>
+ <Liquid_Heat_Capacity_Tmin>113.54</Liquid_Heat_Capacity_Tmin>
+ <Liquid_Thermal_Conductivity_Const_A>0.029586</Liquid_Thermal_Conductivity_Const_A>
+ <Liquid_Thermal_Conductivity_Const_B>56.323</Liquid_Thermal_Conductivity_Const_B>
+ <Liquid_Thermal_Conductivity_Const_C>-2.8746</Liquid_Thermal_Conductivity_Const_C>
+ <Liquid_Thermal_Conductivity_Const_D>0.0051627</Liquid_Thermal_Conductivity_Const_D>
+ <Liquid_Thermal_Conductivity_Const_E>-1.7826E-05</Liquid_Thermal_Conductivity_Const_E>
+ <Liquid_Thermal_Conductivity_Tmax>400</Liquid_Thermal_Conductivity_Tmax>
+ <Liquid_Thermal_Conductivity_Tmin>113.54</Liquid_Thermal_Conductivity_Tmin>
+ <Liquid_Viscosity_Const_A>-39.10125</Liquid_Viscosity_Const_A>
+ <Liquid_Viscosity_Const_B>1315.145</Liquid_Viscosity_Const_B>
+ <Liquid_Viscosity_Const_C>4.876982</Liquid_Viscosity_Const_C>
+ <Liquid_Viscosity_Const_D>-2.03993E-05</Liquid_Viscosity_Const_D>
+ <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+ <LiquidDensityEquation>105</LiquidDensityEquation>
+ <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
+ <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
+ <LiquidViscosityEquation>101</LiquidViscosityEquation>
+ <Molar_Weight>58.1222</Molar_Weight>
+ <MolarVolume_k1i>0</MolarVolume_k1i>
+ <MolarVolume_k2i>0</MolarVolume_k2i>
+ <MolarVolume_k3i>0</MolarVolume_k3i>
+ <MolarVolume_v2i>0</MolarVolume_v2i>
+ <MolarVolume_v3i>0</MolarVolume_v3i>
+ <Name>Isobutane</Name>
+ <NBP>261.34</NBP>
+ <NegativeIon></NegativeIon>
+ <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+ <Normal_Boiling_Point>261.34</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>CC(C)C</SMILES>
+ <Solid_Density_Const_A>15.956</Solid_Density_Const_A>
+ <Solid_Density_Const_B>-0.015646</Solid_Density_Const_B>
+ <Solid_Density_Const_C>0</Solid_Density_Const_C>
+ <Solid_Density_Const_D>0</Solid_Density_Const_D>
+ <Solid_Density_Const_E>0</Solid_Density_Const_E>
+ <Solid_Density_Tmax>113.54</Solid_Density_Tmax>
+ <Solid_Density_Tmin>45.42</Solid_Density_Tmin>
+ <Solid_Heat_Capacity_Const_A>-58597</Solid_Heat_Capacity_Const_A>
+ <Solid_Heat_Capacity_Const_B>5767.7</Solid_Heat_Capacity_Const_B>
+ <Solid_Heat_Capacity_Const_C>-111.79</Solid_Heat_Capacity_Const_C>
+ <Solid_Heat_Capacity_Const_D>0.90616</Solid_Heat_Capacity_Const_D>
+ <Solid_Heat_Capacity_Const_E>-0.0024065</Solid_Heat_Capacity_Const_E>
+ <Solid_Heat_Capacity_Tmax>107</Solid_Heat_Capacity_Tmax>
+ <Solid_Heat_Capacity_Tmin>77</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>-0.007942</Surface_Tension_Const_A>
+ <Surface_Tension_Const_B>27.727</Surface_Tension_Const_B>
+ <Surface_Tension_Const_C>-3.375</Surface_Tension_Const_C>
+ <Surface_Tension_Const_D>0.0010263</Surface_Tension_Const_D>
+ <Surface_Tension_Const_E>-1.1845E-05</Surface_Tension_Const_E>
+ <Surface_Tension_Tmax>407.8</Surface_Tension_Tmax>
+ <Surface_Tension_Tmin>113.54</Surface_Tension_Tmin>
+ <SurfaceTensionEquation>16</SurfaceTensionEquation>
+ <TemperatureOfFusion>113.54</TemperatureOfFusion>
+ <UNIQUAC_Q>2.772</UNIQUAC_Q>
+ <UNIQUAC_R>3.1502</UNIQUAC_R>
+ <Vapor_Pressure_Constant_A>70.58866</Vapor_Pressure_Constant_A>
+ <Vapor_Pressure_Constant_B>-4298.161</Vapor_Pressure_Constant_B>
+ <Vapor_Pressure_Constant_C>-7.798635</Vapor_Pressure_Constant_C>
+ <Vapor_Pressure_Constant_D>1.16E-05</Vapor_Pressure_Constant_D>
+ <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+ <Vapor_Pressure_TMAX>408</Vapor_Pressure_TMAX>
+ <Vapor_Pressure_TMIN>113.54</Vapor_Pressure_TMIN>
+ <Vapor_Thermal_Conductivity_Const_A>0.091178</Vapor_Thermal_Conductivity_Const_A>
+ <Vapor_Thermal_Conductivity_Const_B>0.18264</Vapor_Thermal_Conductivity_Const_B>
+ <Vapor_Thermal_Conductivity_Const_C>626.56</Vapor_Thermal_Conductivity_Const_C>
+ <Vapor_Thermal_Conductivity_Const_D>1124600</Vapor_Thermal_Conductivity_Const_D>
+ <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
+ <Vapor_Thermal_Conductivity_Tmax>1000</Vapor_Thermal_Conductivity_Tmax>
+ <Vapor_Thermal_Conductivity_Tmin>113.54</Vapor_Thermal_Conductivity_Tmin>
+ <Vapor_Viscosity_Const_A>3.951E-08</Vapor_Viscosity_Const_A>
+ <Vapor_Viscosity_Const_B>0.90975</Vapor_Viscosity_Const_B>
+ <Vapor_Viscosity_Const_C>-52.076</Vapor_Viscosity_Const_C>
+ <Vapor_Viscosity_Const_D>8625.4</Vapor_Viscosity_Const_D>
+ <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+ <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
+ <Vapor_Viscosity_Tmin>150</Vapor_Viscosity_Tmin>
+ <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+ <VaporPressureEquation>101</VaporPressureEquation>
+ <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+ <VaporViscosityEquation>102</VaporViscosityEquation>
+ <Z_Rackett>0.275</Z_Rackett>
+ <FullerDiffusionVolume>86.7</FullerDiffusionVolume>
+ <LennardJonesDiameter>5.553216E-10</LennardJonesDiameter>
+ <LennardJonesEnergy>265.4452</LennardJonesEnergy>
+ <Parachor>0.0339</Parachor>
+ <Tag></Tag>
+ <COSTALD_SRK_Acentric_Factor>0.1825</COSTALD_SRK_Acentric_Factor>
+ <COSTALD_Characteristic_Volume>0.25683</COSTALD_Characteristic_Volume>
+ <IsSolid>false</IsSolid>
+ <ChemSepFamily>2</ChemSepFamily>
+ <Vapor_Pressure_Regression_Fit>0</Vapor_Pressure_Regression_Fit>
+ <Vapor_Pressure_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Vapor_Pressure_Tabular_Data>
+ <Ideal_Gas_Heat_Capacity_Regression_Fit>0</Ideal_Gas_Heat_Capacity_Regression_Fit>
+ <Ideal_Gas_Heat_Capacity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Ideal_Gas_Heat_Capacity_Tabular_Data>
+ <Liquid_Viscosity_Regression_Fit>0</Liquid_Viscosity_Regression_Fit>
+ <Liquid_Viscosity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Liquid_Viscosity_Tabular_Data>
+ <Liquid_Density_Regression_Fit>0</Liquid_Density_Regression_Fit>
+ <Liquid_Density_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
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+ <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>1333-74-0</CAS_Number>
+ <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
+ <Chao_Seader_Liquid_Molar_Volume>31</Chao_Seader_Liquid_Molar_Volume>
+ <Chao_Seader_Solubility_Parameter>0.00158781835225</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <Critical_Compressibility>0.305</Critical_Compressibility>
+ <Critical_Pressure>1313000</Critical_Pressure>
+ <Critical_Temperature>33.19</Critical_Temperature>
+ <Critical_Volume>0.064147</Critical_Volume>
+ <CurrentDB>ChemSep</CurrentDB>
+ <Dipole_Moment>0</Dipole_Moment>
+ <Electrolyte_Cp0>0</Electrolyte_Cp0>
+ <Electrolyte_DelGF>0</Electrolyte_DelGF>
+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
+ <EnthalpyOfFusionAtTf>0.1171</EnthalpyOfFusionAtTf>
+ <Formula>H2</Formula>
+ <HVap_A>1534700</HVap_A>
+ <HVap_B>3.214</HVap_B>
+ <HVap_C>-8.4567</HVap_C>
+ <HVap_D>8.4646</HVap_D>
+ <HVap_E>-2.8057</HVap_E>
+ <HVap_TMAX>32.62</HVap_TMAX>
+ <HVap_TMIN>13.95</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>902</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>3994.325</Ideal_Gas_Heat_Capacity_Const_A>
+ <Ideal_Gas_Heat_Capacity_Const_B>-48.69006</Ideal_Gas_Heat_Capacity_Const_B>
+ <Ideal_Gas_Heat_Capacity_Const_C>10.36209</Ideal_Gas_Heat_Capacity_Const_C>
+ <Ideal_Gas_Heat_Capacity_Const_D>-0.000340144</Ideal_Gas_Heat_Capacity_Const_D>
+ <Ideal_Gas_Heat_Capacity_Const_E>1.960333E-07</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>16</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>
+ <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>2.9613</Liquid_Density_Const_A>
+ <Liquid_Density_Const_B>0.25981</Liquid_Density_Const_B>
+ <Liquid_Density_Const_C>33.19</Liquid_Density_Const_C>
+ <Liquid_Density_Const_D>0.19104</Liquid_Density_Const_D>
+ <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+ <Liquid_Density_Tmax>33.18</Liquid_Density_Tmax>
+ <Liquid_Density_Tmin>13.84</Liquid_Density_Tmin>
+ <Liquid_Heat_Capacity_Const_A>14510</Liquid_Heat_Capacity_Const_A>
+ <Liquid_Heat_Capacity_Const_B>-1191.1</Liquid_Heat_Capacity_Const_B>
+ <Liquid_Heat_Capacity_Const_C>156.51</Liquid_Heat_Capacity_Const_C>
+ <Liquid_Heat_Capacity_Const_D>-6.1773</Liquid_Heat_Capacity_Const_D>
+ <Liquid_Heat_Capacity_Const_E>0.087907</Liquid_Heat_Capacity_Const_E>
+ <Liquid_Heat_Capacity_Tmax>32</Liquid_Heat_Capacity_Tmax>
+ <Liquid_Heat_Capacity_Tmin>13.84</Liquid_Heat_Capacity_Tmin>
+ <Liquid_Thermal_Conductivity_Const_A>-0.34238</Liquid_Thermal_Conductivity_Const_A>
+ <Liquid_Thermal_Conductivity_Const_B>-4.3002</Liquid_Thermal_Conductivity_Const_B>
+ <Liquid_Thermal_Conductivity_Const_C>-0.53814</Liquid_Thermal_Conductivity_Const_C>
+ <Liquid_Thermal_Conductivity_Const_D>0.0011639</Liquid_Thermal_Conductivity_Const_D>
+ <Liquid_Thermal_Conductivity_Const_E>-0.00021792</Liquid_Thermal_Conductivity_Const_E>
+ <Liquid_Thermal_Conductivity_Tmax>31</Liquid_Thermal_Conductivity_Tmax>
+ <Liquid_Thermal_Conductivity_Tmin>13.84</Liquid_Thermal_Conductivity_Tmin>
+ <Liquid_Viscosity_Const_A>-32.531</Liquid_Viscosity_Const_A>
+ <Liquid_Viscosity_Const_B>97.304</Liquid_Viscosity_Const_B>
+ <Liquid_Viscosity_Const_C>5.9178</Liquid_Viscosity_Const_C>
+ <Liquid_Viscosity_Const_D>-0.0031563</Liquid_Viscosity_Const_D>
+ <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+ <LiquidDensityEquation>105</LiquidDensityEquation>
+ <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
+ <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
+ <LiquidViscosityEquation>101</LiquidViscosityEquation>
+ <Molar_Weight>2.01588</Molar_Weight>
+ <MolarVolume_k1i>0</MolarVolume_k1i>
+ <MolarVolume_k2i>0</MolarVolume_k2i>
+ <MolarVolume_k3i>0</MolarVolume_k3i>
+ <MolarVolume_v2i>0</MolarVolume_v2i>
+ <MolarVolume_v3i>0</MolarVolume_v3i>
+ <Name>Hydrogen</Name>
+ <NBP>20.39</NBP>
+ <NegativeIon></NegativeIon>
+ <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+ <Normal_Boiling_Point>20.39</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>[H][H]</SMILES>
+ <Solid_Density_Const_A>0</Solid_Density_Const_A>
+ <Solid_Density_Const_B>0</Solid_Density_Const_B>
+ <Solid_Density_Const_C>0</Solid_Density_Const_C>
+ <Solid_Density_Const_D>0</Solid_Density_Const_D>
+ <Solid_Density_Const_E>0</Solid_Density_Const_E>
+ <Solid_Density_Tmax>0</Solid_Density_Tmax>
+ <Solid_Density_Tmin>0</Solid_Density_Tmin>
+ <Solid_Heat_Capacity_Const_A>5730</Solid_Heat_Capacity_Const_A>
+ <Solid_Heat_Capacity_Const_B>-1.3847E-11</Solid_Heat_Capacity_Const_B>
+ <Solid_Heat_Capacity_Const_C>1.1605E-12</Solid_Heat_Capacity_Const_C>
+ <Solid_Heat_Capacity_Const_D>-1.2321E-13</Solid_Heat_Capacity_Const_D>
+ <Solid_Heat_Capacity_Const_E>4.114E-15</Solid_Heat_Capacity_Const_E>
+ <Solid_Heat_Capacity_Tmax>23.45</Solid_Heat_Capacity_Tmax>
+ <Solid_Heat_Capacity_Tmin>13.95</Solid_Heat_Capacity_Tmin>
+ <SolidDensityAtTs>0</SolidDensityAtTs>
+ <SolidDensityEquation></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>-0.003232</Surface_Tension_Const_A>
+ <Surface_Tension_Const_B>1.9865</Surface_Tension_Const_B>
+ <Surface_Tension_Const_C>-5.0915</Surface_Tension_Const_C>
+ <Surface_Tension_Const_D>-0.00046122</Surface_Tension_Const_D>
+ <Surface_Tension_Const_E>-0.00062971</Surface_Tension_Const_E>
+ <Surface_Tension_Tmax>32.18</Surface_Tension_Tmax>
+ <Surface_Tension_Tmin>13.95</Surface_Tension_Tmin>
+ <SurfaceTensionEquation>16</SurfaceTensionEquation>
+ <TemperatureOfFusion>13.95</TemperatureOfFusion>
+ <UNIQUAC_Q>0.5516</UNIQUAC_Q>
+ <UNIQUAC_R>0.4092</UNIQUAC_R>
+ <Vapor_Pressure_Constant_A>13.05</Vapor_Pressure_Constant_A>
+ <Vapor_Pressure_Constant_B>-97.534</Vapor_Pressure_Constant_B>
+ <Vapor_Pressure_Constant_C>1.0355</Vapor_Pressure_Constant_C>
+ <Vapor_Pressure_Constant_D>0.00031816</Vapor_Pressure_Constant_D>
+ <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+ <Vapor_Pressure_TMAX>33.19</Vapor_Pressure_TMAX>
+ <Vapor_Pressure_TMIN>13.08</Vapor_Pressure_TMIN>
+ <Vapor_Thermal_Conductivity_Const_A>0.0026851</Vapor_Thermal_Conductivity_Const_A>
+ <Vapor_Thermal_Conductivity_Const_B>0.74366</Vapor_Thermal_Conductivity_Const_B>
+ <Vapor_Thermal_Conductivity_Const_C>13.289</Vapor_Thermal_Conductivity_Const_C>
+ <Vapor_Thermal_Conductivity_Const_D>-31.305</Vapor_Thermal_Conductivity_Const_D>
+ <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
+ <Vapor_Thermal_Conductivity_Tmax>1600</Vapor_Thermal_Conductivity_Tmax>
+ <Vapor_Thermal_Conductivity_Tmin>10</Vapor_Thermal_Conductivity_Tmin>
+ <Vapor_Viscosity_Const_A>1.7916E-07</Vapor_Viscosity_Const_A>
+ <Vapor_Viscosity_Const_B>0.68557</Vapor_Viscosity_Const_B>
+ <Vapor_Viscosity_Const_C>-0.51413</Vapor_Viscosity_Const_C>
+ <Vapor_Viscosity_Const_D>132.61</Vapor_Viscosity_Const_D>
+ <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+ <Vapor_Viscosity_Tmax>2000</Vapor_Viscosity_Tmax>
+ <Vapor_Viscosity_Tmin>13.95</Vapor_Viscosity_Tmin>
+ <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+ <VaporPressureEquation>101</VaporPressureEquation>
+ <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+ <VaporViscosityEquation>102</VaporViscosityEquation>
+ <Z_Rackett>0.3139</Z_Rackett>
+ <FullerDiffusionVolume>6.12</FullerDiffusionVolume>
+ <LennardJonesDiameter>3.105589E-10</LennardJonesDiameter>
+ <LennardJonesEnergy>30.15782</LennardJonesEnergy>
+ <Parachor>0.0061</Parachor>
+ <Tag></Tag>
+ <COSTALD_SRK_Acentric_Factor>-0.2324</COSTALD_SRK_Acentric_Factor>
+ <COSTALD_Characteristic_Volume>0.06424</COSTALD_Characteristic_Volume>
+ <IsSolid>false</IsSolid>
+ <ChemSepFamily>74</ChemSepFamily>
+ <Vapor_Pressure_Regression_Fit>0</Vapor_Pressure_Regression_Fit>
+ <Vapor_Pressure_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Vapor_Pressure_Tabular_Data>
+ <Ideal_Gas_Heat_Capacity_Regression_Fit>0</Ideal_Gas_Heat_Capacity_Regression_Fit>
+ <Ideal_Gas_Heat_Capacity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Ideal_Gas_Heat_Capacity_Tabular_Data>
+ <Liquid_Viscosity_Regression_Fit>0</Liquid_Viscosity_Regression_Fit>
+ <Liquid_Viscosity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Liquid_Viscosity_Tabular_Data>
+ <Liquid_Density_Regression_Fit>0</Liquid_Density_Regression_Fit>
+ <Liquid_Density_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Liquid_Density_Tabular_Data>
+ <Liquid_Heat_Capacity_Regression_Fit>0</Liquid_Heat_Capacity_Regression_Fit>
+ <Liquid_Heat_Capacity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Liquid_Heat_Capacity_Tabular_Data>
+ <Liquid_Thermal_Conductivity_Regression_Fit>0</Liquid_Thermal_Conductivity_Regression_Fit>
+ <Liquid_Thermal_Conductivity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Liquid_Thermal_Conductivity_Tabular_Data>
+ <Vapor_Thermal_Conductivity_Regression_Fit>0</Vapor_Thermal_Conductivity_Regression_Fit>
+ <Vapor_Thermal_Conductivity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Vapor_Thermal_Conductivity_Tabular_Data>
+ <Vapor_Viscosity_Regression_Fit>0</Vapor_Viscosity_Regression_Fit>
+ <Vapor_Viscosity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Vapor_Viscosity_Tabular_Data>
+ <Solid_Density_Regression_Fit>0</Solid_Density_Regression_Fit>
+ <Solid_Density_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Solid_Density_Tabular_Data>
+ <Surface_Tension_Regression_Fit>0</Surface_Tension_Regression_Fit>
+ <Surface_Tension_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Surface_Tension_Tabular_Data>
+ <Solid_Heat_Capacity_Regression_Fit>0</Solid_Heat_Capacity_Regression_Fit>
+ <Solid_Heat_Capacity_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Solid_Heat_Capacity_Tabular_Data>
+ <Enthalpy_Of_Vaporization_Regression_Fit>0</Enthalpy_Of_Vaporization_Regression_Fit>
+ <Enthalpy_Of_Vaporization_Tabular_Data>
+ <Type>DWSIM.SharedClasses.TabularData</Type>
+ <XName></XName>
+ <YName></YName>
+ <XUnit></XUnit>
+ <YUnit></YUnit>
+ <XData />
+ <YData />
+ <Source></Source>
+ <Comments></Comments>
+ </Enthalpy_Of_Vaporization_Tabular_Data>
+ <StandardHeatOfCombustion_LHV>-119957.537154989</StandardHeatOfCombustion_LHV>
+ <DynamicProperties />
+ <UNIFACGroups />
+ <MODFACGroups />
+ <NISTMODFACGroups />
+ <Elements>
+ <Item Name="H" Value="2" />
+ </Elements>
+ </Compound>
+ </Compounds>
+ <ReactionSets>
+ <ReactionSet>
+ <ID>DefaultSet</ID>
+ <Name>Default Set</Name>
+ <Description>Default Reaction Set</Description>
+ <Reactions>
+ <Reaction Key="ff2db60c-ff59-401a-8ee5-c6a658130587" ReactionID="ff2db60c-ff59-401a-8ee5-c6a658130587" Rank="0" IsActive="true" />
+ </Reactions>
+ </ReactionSet>
+ </ReactionSets>
+ <Reactions>
+ <Reaction>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Reaction</Type>
+ <BaseReactant>Isobutane</BaseReactant>
+ <Description></Description>
+ <Equation>CH3CH(CH3)CH3 <--> CH2C(CH3)2 + H2 </Equation>
+ <ID>ff2db60c-ff59-401a-8ee5-c6a658130587</ID>
+ <Name>rxn1</Name>
+ <ReactionBasis>PartialPress</ReactionBasis>
+ <ReactionHeat>117890</ReactionHeat>
+ <ReactionHeatCO>0</ReactionHeatCO>
+ <ReactionPhase>Vapor</ReactionPhase>
+ <ReactionType>Heterogeneous_Catalytic</ReactionType>
+ <StoichBalance>0</StoichBalance>
+ <A_Forward>0</A_Forward>
+ <A_Reverse>0</A_Reverse>
+ <Approach>0</Approach>
+ <ConcUnit>bar</ConcUnit>
+ <ConstantKeqValue>0</ConstantKeqValue>
+ <E_Forward>0</E_Forward>
+ <E_Reverse>0</E_Reverse>
+ <Expression></Expression>
+ <KExprType>Gibbs</KExprType>
+ <Kvalue>0</Kvalue>
+ <Rate>0</Rate>
+ <RateEquationDenominator>1 + (6.34E-2 * exp(-31.59 / (8.314 * (T + 273.15))) * R1) + (2.41E-4 * exp(-64.78 / (8.314 * (T + 273.15))) * P1) + (8.20E-5 * exp(-57.90 / (8.314 * (T + 273.15))) * P2)</RateEquationDenominator>
+ <RateEquationNumerator>(1.67E+6 * exp(-101.31 / (8.314 * (T + 273.15)))) * R1</RateEquationNumerator>
+ <ReactionGibbsEnergy>79520.0000000002</ReactionGibbsEnergy>
+ <Tmax>2000</Tmax>
+ <Tmin>0</Tmin>
+ <VelUnit>kmol/[kg.s]</VelUnit>
+ <ReactionKinFwdType>Arrhenius</ReactionKinFwdType>
+ <ReactionKinRevType>Arrhenius</ReactionKinRevType>
+ <ReactionKinFwdExpression></ReactionKinFwdExpression>
+ <ReactionKinRevExpression></ReactionKinRevExpression>
+ <E_Forward_Unit>J/mol</E_Forward_Unit>
+ <E_Reverse_Unit>J/mol</E_Reverse_Unit>
+ <ReactionKinetics>Expression</ReactionKinetics>
+ <ScriptTitle></ScriptTitle>
+ <EquilibriumReactionBasisUnits>Pa</EquilibriumReactionBasisUnits>
+ <Compounds>
+ <Compound Name="Isobutane" StoichCoeff="-1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="true" />
+ <Compound Name="Isobutene" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
+ <Compound Name="Hydrogen" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
+ </Compounds>
+ </Reaction>
+ </Reactions>
+ <StoredSolutions />
+ <DynamicsManager>
+ <Type>DWSIM.DynamicsManager.Manager</Type>
+ <Description></Description>
+ <CurrentSchedule></CurrentSchedule>
+ <ScheduleList />
+ <EventSetList />
+ <IntegratorList />
+ </DynamicsManager>
+ <OptimizationCases>
+ <OptimizationCase>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.OptimizationCase</Type>
+ <name>optcase0</name>
+ <description></description>
+ <stats></stats>
+ <solvm>AL_BRENT</solvm>
+ <maxits>100</maxits>
+ <tolerance>1E-06</tolerance>
+ <epsX>0.001</epsX>
+ <epsF>0.001</epsF>
+ <epsG>0.001</epsG>
+ <epsilon>0.001</epsilon>
+ <barriermultiplier>0.0001</barriermultiplier>
+ <numdevscheme>2</numdevscheme>
+ <boundvariables>false</boundvariables>
+ <objfunctype>Variable</objfunctype>
+ <type>Minimization</type>
+ <expression></expression>
+ <Variables />
+ </OptimizationCase>
+ </OptimizationCases>
+ <SensitivityAnalysis>
+ <SensitivityAnalysisCase>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SensitivityAnalysisCase</Type>
+ <iv1>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
+ <objectID></objectID>
+ <objectTAG></objectTAG>
+ <propID></propID>
+ <unit></unit>
+ <points>5</points>
+ <name></name>
+ <id></id>
+ <currentvalue>0</currentvalue>
+ </iv1>
+ <iv2>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
+ <objectID></objectID>
+ <objectTAG></objectTAG>
+ <propID></propID>
+ <unit></unit>
+ <points>5</points>
+ <name></name>
+ <id></id>
+ <currentvalue>0</currentvalue>
+ </iv2>
+ <dv>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
+ <objectID></objectID>
+ <objectTAG></objectTAG>
+ <propID></propID>
+ <unit></unit>
+ <points>5</points>
+ <name></name>
+ <id></id>
+ <currentvalue>0</currentvalue>
+ </dv>
+ <name>SACase0</name>
+ <description></description>
+ <stats></stats>
+ <numvar>1</numvar>
+ <depvartype>Variable</depvartype>
+ <expression></expression>
+ <IV1>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
+ <objectID></objectID>
+ <objectTAG></objectTAG>
+ <propID></propID>
+ <unit></unit>
+ <points>5</points>
+ <name></name>
+ <id></id>
+ <currentvalue>0</currentvalue>
+ </IV1>
+ <IV2>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
+ <objectID></objectID>
+ <objectTAG></objectTAG>
+ <propID></propID>
+ <unit></unit>
+ <points>5</points>
+ <name></name>
+ <id></id>
+ <currentvalue>0</currentvalue>
+ </IV2>
+ <DV>
+ <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
+ <objectID></objectID>
+ <objectTAG></objectTAG>
+ <propID></propID>
+ <unit></unit>
+ <points>5</points>
+ <name></name>
+ <id></id>
+ <currentvalue>0</currentvalue>
+ </DV>
+ <Variables />
+ <DepVariables />
+ </SensitivityAnalysisCase>
+ </SensitivityAnalysis>
+ <PetroleumAssays />
+ <WatchItems />
+ <ScriptItems />
+ <ChartItems />
+ <ParticleSizeDistributions />
+ <Spreadsheet>
+ <RGFData>{"MAIN":"{\"?xml\":{\"@version\":\"1.0\"},\"grid\":{\"@xmlns:xsd\":\"http://www.w3.org/2001/XMLSchema\",\"@xmlns:xsi\":\"http://www.w3.org/2001/XMLSchema-instance\",\"head\":{\"meta\":{\"culture\":\"en-US\",\"editor\":\"ReoGrid Core\",\"core-ver\":\"2.1.0.0\"},\"rows\":\"65536\",\"cols\":\"100\",\"default-row-height\":\"20\",\"default-col-width\":\"70\",\"focus-forward-direction\":\"down\",\"settings\":{\"@meta\":\"30475026398\"},\"script\":null},\"style\":{\"@font\":\"Arial\",\"@font-size\":\"10\",\"@align\":\"general\",\"@valign\":\"middle\"},\"rows\":null,\"cols\":null,\"v-borders\":null,\"h-borders\":null,\"cells\":null}}"}</RGFData>
+ </Spreadsheet>
+ <PanelLayout><?xml version="1.0" encoding="utf-8"?>
+<!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.-->
+<!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!-->
+<DockPanel FormatVersion="1.0" DockLeftPortion="675" DockRightPortion="0.203007518796992" DockTopPortion="0.25" DockBottomPortion="0.152227705943669" ActiveDocumentPane="0" ActivePane="0">
+ <Contents Count="12">
+ <Content ID="0" PersistString="DWSIM.LogPanel" AutoHidePortion="0.152227705943669" IsHidden="True" IsFloat="False" />
+ <Content ID="1" PersistString="DWSIM.MaterialStreamPanel" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
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+ <Content ID="3" PersistString="DWSIM.FormCharts" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
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+ <Content ID="6" PersistString="DWSIM.FormFileExplorer" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
+ <Content ID="7" PersistString="DWSIM.FormNewSpreadsheet" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
+ <Content ID="8" PersistString="DWSIM.FlowsheetSurface_SkiaSharp" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
+ <Content ID="9" PersistString="DWSIM.FormScript" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
+ <Content ID="10" PersistString="DWSIM.ProFeatures.FormGHG" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
+ <Content ID="11" PersistString="DWSIM.ProFeatures.FormCosting" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
+ </Contents>
+ <Panes Count="5">
+ <Pane ID="0" DockState="Document" ActiveContent="8">
+ <Contents Count="9">
+ <Content ID="0" RefID="6" />
+ <Content ID="1" RefID="4" />
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+ <Content ID="4" RefID="7" />
+ <Content ID="5" RefID="8" />
+ <Content ID="6" RefID="9" />
+ <Content ID="7" RefID="10" />
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+ </Contents>
+ </Pane>
+ <Pane ID="1" DockState="DockBottom" ActiveContent="-1">
+ <Contents Count="1">
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+ </Pane>
+ <Pane ID="2" DockState="DockBottom" ActiveContent="-1">
+ <Contents Count="1">
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+ </Pane>
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+ </Pane>
+ <Pane ID="4" DockState="DockBottom" ActiveContent="-1">
+ <Contents Count="1">
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+ </Contents>
+ </Pane>
+ </Panes>
+ <DockWindows>
+ <DockWindow ID="0" DockState="Document" ZOrderIndex="1">
+ <NestedPanes Count="1">
+ <Pane ID="0" RefID="0" PrevPane="-1" Alignment="Right" Proportion="0.5" />
+ </NestedPanes>
+ </DockWindow>
+ <DockWindow ID="1" DockState="DockLeft" ZOrderIndex="2">
+ <NestedPanes Count="0" />
+ </DockWindow>
+ <DockWindow ID="2" DockState="DockRight" ZOrderIndex="3">
+ <NestedPanes Count="0" />
+ </DockWindow>
+ <DockWindow ID="3" DockState="DockTop" ZOrderIndex="5">
+ <NestedPanes Count="0" />
+ </DockWindow>
+ <DockWindow ID="4" DockState="DockBottom" ZOrderIndex="4">
+ <NestedPanes Count="3">
+ <Pane ID="0" RefID="1" PrevPane="-1" Alignment="Right" Proportion="0.5" />
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+ </NestedPanes>
+ </DockWindow>
+ </DockWindows>
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+ </NestedPanes>
+ </FloatWindow>
+ </FloatWindows>
+</DockPanel></PanelLayout>
+ <MessagesLog>
+ <Message>[2/15/2025 10:05:28 AM] The flowsheet was calculated successfully. [0.393s]</Message>
+ <Message>[2/15/2025 10:05:39 AM] The flowsheet was calculated successfully. [0.005565s]</Message>
+ <Message>[2/15/2025 10:05:42 AM] The flowsheet was calculated successfully. [0.02188s]</Message>
+ <Message>[2/15/2025 10:06:01 AM] 2: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:01 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:01 AM] The flowsheet was calculated successfully. [0.005778s]</Message>
+ <Message>[2/15/2025 10:06:03 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:03 AM] The flowsheet was calculated successfully. [0.01177s]</Message>
+ <Message>[2/15/2025 10:06:18 AM] The flowsheet was calculated successfully. [0.003548s]</Message>
+ <Message>[2/15/2025 10:06:23 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:23 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:23 AM] The flowsheet was calculated successfully. [0.01476s]</Message>
+ <Message>[2/15/2025 10:06:28 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:28 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:28 AM] The flowsheet was calculated successfully. [0.003794s]</Message>
+ <Message>[2/15/2025 10:06:31 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:31 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:31 AM] The flowsheet was calculated successfully. [0.004002s]</Message>
+ <Message>[2/15/2025 10:06:33 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:33 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:33 AM] The flowsheet was calculated successfully. [0.004006s]</Message>
+ <Message>[2/15/2025 10:06:41 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:41 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:41 AM] The flowsheet was calculated successfully. [0.01041s]</Message>
+ <Message>[2/15/2025 10:06:44 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:44 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:06:44 AM] The flowsheet was calculated successfully. [0.003186s]</Message>
+ <Message>[2/15/2025 10:08:08 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:08:08 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:08:08 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:08:08 AM] 8: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:08:08 AM] The flowsheet was calculated successfully. [4.191s]</Message>
+ <Message>[2/15/2025 10:08:54 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:08:54 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:08:55 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:08:55 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:09:04 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+ <Message>[2/15/2025 10:09:04 AM] Error in 'CS-1': Calculated negative molar flow for stream 8, compound Hydrogen [-7.105427357601E-15 mol/s]. (ComponentSeparator.vb, 199)</Message>
+ <Message>[2/15/2025 10:09:25 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:09:25 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:09:26 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:09:26 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:09:27 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:09:27 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:09:31 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:09:31 AM] The flowsheet was calculated successfully. [8.54s]</Message>
+ <Message>[2/15/2025 10:09:42 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:09:42 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:09:42 AM] The calculator is busy, please wait...</Message>
+ <Message>[2/15/2025 10:09:42 AM] Dynamic Mode is currently enabled.</Message>
+ <Message>[2/15/2025 10:09:48 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:09:48 AM] The flowsheet was calculated successfully. [8.447s]</Message>
+ <Message>[2/15/2025 10:10:13 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:10:13 AM] The flowsheet was calculated successfully. [8.466s]</Message>
+ <Message>[2/15/2025 10:10:43 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[2/15/2025 10:10:43 AM] The flowsheet was calculated successfully. [8.464s]</Message>
+ <Message>[3/8/2025 9:06:13 AM] File C:\Users\aruls\OneDrive\Desktop\Recent_works\flowsheeting\Flowsheet.dwxml saved successfully.</Message>
+ <Message>[3/8/2025 10:35:58 AM] S-02: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[3/8/2025 10:35:59 AM] S-05: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[3/8/2025 10:35:59 AM] The flowsheet was calculated successfully. [9.024s]</Message>
+ <Message>[3/8/2025 5:25:34 PM] S-02: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[3/8/2025 5:25:34 PM] S-05: Single-compound Stream detected. Switching to PH Flash</Message>
+ <Message>[3/8/2025 5:25:34 PM] The flowsheet was calculated successfully. [8.971s]</Message>
+ </MessagesLog>
+ <Results>
+ <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetResults</Type>
+ <TotalCAPEX>0</TotalCAPEX>
+ <TotalOPEX>0</TotalOPEX>
+ <ResidualMassBalance>-5.81246162312254E-12</ResidualMassBalance>
+ <TotalEnergyBalance>-5032.08577856815</TotalEnergyBalance>
+ <AdditionalResults />
+ </Results>
+ <GHGCompositions />
+</DWSIM_Simulation_Data>
\ No newline at end of file diff --git a/Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Abstract_DiethyleneGlycol.pdf b/Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Abstract_DiethyleneGlycol.pdf Binary files differnew file mode 100644 index 0000000..4130a30 --- /dev/null +++ b/Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Abstract_DiethyleneGlycol.pdf diff --git a/Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Diethylene_Glycol.dwxmz b/Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Diethylene_Glycol.dwxmz Binary files differnew file mode 100644 index 0000000..bd2e7b9 --- /dev/null +++ b/Production_Of_Diethylene_Glycol_Using_Ethylene_As_Raw_Material_By_Mr_Parth_Manish_Dani/Diethylene_Glycol.dwxmz |