Added(A)/Deleted(D) following Flowsheet file

R "Low\342\200\224temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Abstract.pdf" -> Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Abstract.pdf R "Low\342\200\224temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Flowsheet.dwxmz" -> Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Flowsheet.dwxmz A Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/README.txt A Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf A Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
author: Sashi20 2023-12-16 00:20:16 +0550
committer: Sashi20 2023-12-16 00:20:16 +0550
commit: 1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142 (patch)
tree: 122cf478e9b208a144cd3a8e5be249ba3c59420a
parent: 43bb5bc5978d5bc5ff75c156993ac7710d515502 (diff)
download: DWSIM-Flowsheets-1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142.tar.gz
DWSIM-Flowsheets-1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142.tar.bz2
DWSIM-Flowsheets-1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142.zip
5 files changed, 11455 insertions, 0 deletions
diff --git a/Low—temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Abstract.pdf b/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Abstract.pdf
index 296fde2..296fde2 100644
--- a/Low—temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Abstract.pdf
+++ b/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Abstract.pdf
diff --git a/Low—temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Flowsheet.dwxmz b/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Flowsheet.dwxmz
index f29d67e..f29d67e 100644
--- a/Low—temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Flowsheet.dwxmz
+++ b/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/Flowsheet.dwxmz
diff --git a/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/README.txt b/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/README.txt
new file mode 100644
index 0000000..fdbac83
--- /dev/null
+++ b/Low-Temperature_Hybrid_Geothermal-Solar_Power_Plant_By_Mr_Amirhossein_Hosseinzadeh/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Low-Temperature Hybrid Geothermal-Solar Power Plant
+Proposar Name: Mr Amirhossein Hosseinzadeh
+University: Amirkabir University of Technology (Tehran Polytechnique)
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf
new file mode 100644
index 0000000..1b64801
--- /dev/null
+++ b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf
diff --git a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
new file mode 100644
index 0000000..515f564
--- /dev/null
+++ b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
@@ -0,0 +1,11447 @@
+<?xml version="1.0" encoding="utf-8"?>
+<DWSIM_Simulation_Data>
+  <GeneralInfo>
+    <BuildVersion>8.6.5.0</BuildVersion>
+    <BuildDate>2000-01-06T00:00:00</BuildDate>
+    <OSInfo>Microsoft Windows 11 Home Single Language, Version 10.0.22621.0, Win32NT Platform</OSInfo>
+    <SavedOn>2023-11-13T20:39:22.014771+05:30</SavedOn>
+    <SavedFromClassicUI>true</SavedFromClassicUI>
+  </GeneralInfo>
+  <SimulationObjects>
+    <SimulationObject>
+      <Type>DWSIM.UnitOperations.SpecialOps.Recycle</Type>
+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+      <Converged>true</Converged>
+      <CopyOnStreamDataError>false</CopyOnStreamDataError>
+      <Errors />
+      <Values />
+      <IterationsTaken>2</IterationsTaken>
+      <IterationCount>1</IterationCount>
+      <AccelerationMethod>None</AccelerationMethod>
+      <ConvergenceParameters>
+        <Type>DWSIM.UnitOperations.SpecialOps.Helpers.Recycle.ConvergenceParameters</Type>
+        <Temperatura>0.1</Temperatura>
+        <Pressao>0.1</Pressao>
+        <VazaoMassica>0.01</VazaoMassica>
+        <FracaoVapor>0.01</FracaoVapor>
+        <Entalpia>1</Entalpia>
+        <Entropia>0.01</Entropia>
+        <Composicao>0.001</Composicao>
+      </ConvergenceParameters>
+      <ConvergenceHistory>
+        <Type>DWSIM.UnitOperations.SpecialOps.Helpers.Recycle.ConvergenceHistory</Type>
+      </ConvergenceHistory>
+      <MaximumIterations>50</MaximumIterations>
+      <MobileCompatible>true</MobileCompatible>
+      <ObjectClass>Logical</ObjectClass>
+      <IsDirty>true</IsDirty>
+      <CanUsePreviousResults>false</CanUsePreviousResults>
+      <DynamicsSpec>Pressure</DynamicsSpec>
+      <DynamicsOnly>false</DynamicsOnly>
+      <Visible>true</Visible>
+      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+      <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+      <IsFunctional>true</IsFunctional>
+      <ComponentDescription>Reciclo</ComponentDescription>
+      <ComponentName>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</ComponentName>
+      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+      <Calculated>true</Calculated>
+      <DebugMode>false</DebugMode>
+      <LastUpdated>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</Name>
+      <UserDefinedChartNames />
+      <ProductName>Recycle Block</ProductName>
+      <ProductDescription>Block for connecting tear Material Streams</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <WegPars AccelDelay="2" AccelFreq="4" Qmax="0" Qmin="-20" />
+    </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>-167.71785871462</TotalEnergyFlow>
+      <AtEquilibrium>true</AtEquilibrium>
+      <ComponentDescription>CorrentedeMatria</ComponentDescription>
+      <ComponentName>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</ComponentName>
+      <Name2>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</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>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name>
+      <UserDefinedChartNames />
+      <ProductName>Material Stream</ProductName>
+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
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+      <Phases>
+        <Phase>
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+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <MassFlow>9.93380717989532E-16</MassFlow>
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+              <Name>Acetone</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>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <ComponentName>3-methylhexane</ComponentName>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+          <Properties>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+            <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
+            <molar_internal_energy>4.08001516144059</molar_internal_energy>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>1.08771216295405E-07</PartialPressure>
+              <PartialVolume>17.9016023256588</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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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>Water</Name>
+              <PartialPressure>25682.985167798</PartialPressure>
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+              <DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.942467478041379</MassFraction>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>75642.0148320932</PartialPressure>
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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>
+            <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>3</ID>
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
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+              <Molarity>2.85079554049368E-10</Molarity>
+              <Molality>0</Molality>
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+              <MassFlow>9.93380717989532E-16</MassFlow>
+              <MolarFlow>1.71039157602804E-14</MolarFlow>
+              <Name>Acetone</Name>
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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>Water</ComponentName>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
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+              <MassFlow>0.0415457768509695</MassFlow>
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+              <Name>3-methylhexane</Name>
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+              <DiffusionCoefficient>2.59101048628958E-09</DiffusionCoefficient>
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+              <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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+            <density>802.227353678979</density>
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+            <enthalpyF>-3484.59544673195</enthalpyF>
+            <entropy>0.000423627683257757</entropy>
+            <entropyF>0.000423627682931141</entropyF>
+            <heatCapacityCp>0</heatCapacityCp>
+            <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+            <kinematic_viscosity>7.54356581787694E-07</kinematic_viscosity>
+            <massflow>0.0481312282239006</massflow>
+            <massfraction>1</massfraction>
+            <molar_enthalpy>7.79215837322055</molar_enthalpy>
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+            <molarflow>0.78016833552061</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>61.6933885067027</molecularWeight>
+            <speedOfSound>NaN</speedOfSound>
+            <thermalConductivity>0.139308428645295</thermalConductivity>
+            <viscosity>0.000605165484337862</viscosity>
+            <volumetric_flow>5.99969921284445E-05</volumetric_flow>
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+            <helmholtz_energy>-0.060170843288607</helmholtz_energy>
+            <internal_energy>0.0661337504746934</internal_energy>
+            <isothermal_compressibility>-0.0110018410436479</isothermal_compressibility>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
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+            <idealGasHeatCapacityCp>1.66460606324854</idealGasHeatCapacityCp>
+            <idealGasHeatCapacityRatio>1.08808958782905</idealGasHeatCapacityRatio>
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+              <PetroleumFraction>false</PetroleumFraction>
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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>Acetone</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
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+              <PetroleumFraction>false</PetroleumFraction>
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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>Water</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid2</ComponentName>
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+          <Name>Liquid2</Name>
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+            <helmholtz_energy>0</helmholtz_energy>
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+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+        </Phase>
+        <Phase>
+          <ID>5</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
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+              <PartialVolume>0.0737984191993252</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <Molarity>0</Molarity>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
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+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</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>
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+            <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>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <Molarity>0</Molarity>
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+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</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>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Solid</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Solid</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+      </Phases>
+    </SimulationObject>
+    <SimulationObject>
+      <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
+      <ObjectClass>Exchangers</ObjectClass>
+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
+      <OutletTemperature>298.15</OutletTemperature>
+      <OutletVaporFraction>0</OutletVaporFraction>
+      <CalcMode>OutletTemperature</CalcMode>
+      <Eficiencia>100</Eficiencia>
+      <DeltaT>-70.7602112522569</DeltaT>
+      <DeltaQ>8.93828063257156</DeltaQ>
+      <MobileCompatible>true</MobileCompatible>
+      <ExternalSolverID></ExternalSolverID>
+      <ExternalSolverConfigData></ExternalSolverConfigData>
+      <ComponentDescription>Resfriador</ComponentDescription>
+      <ComponentName>RESF-26c14620-b257-493a-b6d0-b997b40f8564</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>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>RESF-26c14620-b257-493a-b6d0-b997b40f8564</Name>
+      <UserDefinedChartNames />
+      <ProductName>Cooler</ProductName>
+      <ProductDescription>Simple cooler model</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties>
+        <Property>
+          <Name>Flow Conductance</Name>
+          <PropertyType>System.Double</PropertyType>
+          <Data>1.0</Data>
+        </Property>
+        <Property>
+          <Name>Volume</Name>
+          <PropertyType>System.Double</PropertyType>
+          <Data>1.0</Data>
+        </Property>
+        <Property>
+          <Name>Minimum Pressure</Name>
+          <PropertyType>System.Double</PropertyType>
+          <Data>101325.0</Data>
+        </Property>
+        <Property>
+          <Name>Initialize using Inlet Stream</Name>
+          <PropertyType>System.Double</PropertyType>
+          <Data>-1.0</Data>
+        </Property>
+        <Property>
+          <Name>Reset Content</Name>
+          <PropertyType>System.Double</PropertyType>
+          <Data>0.0</Data>
+        </Property>
+      </DynamicProperties>
+      <DynamicPropertiesDescriptions>
+        <Property>
+          <Name>Flow Conductance</Name>
+          <PropertyType>System.String</PropertyType>
+          <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
+        </Property>
+        <Property>
+          <Name>Volume</Name>
+          <PropertyType>System.String</PropertyType>
+          <Data>"Cooler Volume"</Data>
+        </Property>
+        <Property>
+          <Name>Minimum Pressure</Name>
+          <PropertyType>System.String</PropertyType>
+          <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
+        </Property>
+        <Property>
+          <Name>Initialize using Inlet Stream</Name>
+          <PropertyType>System.String</PropertyType>
+          <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
+        </Property>
+        <Property>
+          <Name>Reset Content</Name>
+          <PropertyType>System.String</PropertyType>
+          <Data>"Empties the volume content on the next run."</Data>
+        </Property>
+      </DynamicPropertiesDescriptions>
+      <DynamicPropertiesUnitTypes>
+        <Property>
+          <Name>Flow Conductance</Name>
+          <PropertyType>System.Int64</PropertyType>
+          <Data>67</Data>
+        </Property>
+        <Property>
+          <Name>Volume</Name>
+          <PropertyType>System.Int64</PropertyType>
+          <Data>63</Data>
+        </Property>
+        <Property>
+          <Name>Minimum Pressure</Name>
+          <PropertyType>System.Int64</PropertyType>
+          <Data>46</Data>
+        </Property>
+        <Property>
+          <Name>Initialize using Inlet Stream</Name>
+          <PropertyType>System.Int64</PropertyType>
+          <Data>66</Data>
+        </Property>
+        <Property>
+          <Name>Reset Content</Name>
+          <PropertyType>System.Int64</PropertyType>
+          <Data>66</Data>
+        </Property>
+      </DynamicPropertiesUnitTypes>
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</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>-158.779578082049</TotalEnergyFlow>
+      <AtEquilibrium>true</AtEquilibrium>
+      <ComponentDescription>CorrentedeMatria</ComponentDescription>
+      <ComponentName>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</ComponentName>
+      <Name2>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</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>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name>
+      <UserDefinedChartNames />
+      <ProductName>Material Stream</ProductName>
+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+      <Phases>
+        <Phase>
+          <ID>0</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>2.06390062054607E-14</MassFraction>
+              <MoleFraction>2.1923365742429E-14</MoleFraction>
+              <Molarity>2.6578667110063E-10</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>21.5085411131849</Kvalue>
+              <lnKvalue>3.0684501173247</lnKvalue>
+              <MassFlow>9.93380717989532E-16</MassFlow>
+              <MolarFlow>1.71039157602804E-14</MolarFlow>
+              <Name>Acetone</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.136822840719863</MassFraction>
+              <MoleFraction>0.4685502900383</MoleFraction>
+              <Molarity>5680.44265171835</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0.858622129903028</Kvalue>
+              <lnKvalue>-0.152426349120118</lnKvalue>
+              <MassFlow>0.0065854513729301</MassFlow>
+              <MolarFlow>0.36554809988688</MolarFlow>
+              <Name>Water</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.863177159280117</MassFraction>
+              <MoleFraction>0.53144970996168</MoleFraction>
+              <Molarity>6443.00017285851</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>1.12464517488072</Kvalue>
+              <lnKvalue>0.117467585801286</lnKvalue>
+              <MassFlow>0.0415457768509695</MassFlow>
+              <MolarFlow>0.414620235633715</MolarFlow>
+              <Name>3-methylhexane</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>747.936268215432</density>
+            <enthalpy>185.832777551232</enthalpy>
+            <entropy>0.503734436952633</entropy>
+            <heatCapacityCp>0</heatCapacityCp>
+            <heatCapacityCv>0</heatCapacityCv>
+            <massflow>0.0481312282239006</massflow>
+            <molar_enthalpy>11464.6537427478</molar_enthalpy>
+            <molar_entropy>31.0770843231239</molar_entropy>
+            <molarflow>0.78016833552061</molarflow>
+            <molecularWeight>61.6933885067027</molecularWeight>
+            <pressure>101325</pressure>
+            <surfaceTension>0.0347462890490967</surfaceTension>
+            <temperature>368.910211252257</temperature>
+            <thermalConductivity>0.120307882424234</thermalConductivity>
+            <volumetric_flow>6.43520447788168E-05</volumetric_flow>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.0659014819911475</helmholtz_energy>
+            <internal_energy>185.766876069241</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-4.06568573164734</molar_helmholtz_energy>
+            <molar_internal_energy>11460.5880570162</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>1</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>2.06390062054608E-14</MassFraction>
+              <MoleFraction>2.1923365742429E-14</MoleFraction>
+              <Molarity>2.6578667110063E-10</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>9.9338071798953E-16</MassFlow>
+              <MolarFlow>1.71039157602804E-14</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0829883956543016</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.136822840719863</MassFraction>
+              <MoleFraction>0.468550290038299</MoleFraction>
+              <Molarity>5680.44265171834</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.00658545137293009</MassFlow>
+              <MolarFlow>0.365548099886879</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0187413369026188</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.863177159280117</MassFraction>
+              <MoleFraction>0.531449709961679</MoleFraction>
+              <Molarity>6443.0001728585</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0415457768509694</MassFlow>
+              <MolarFlow>0.414620235633714</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.160163998201726</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>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>0.00132557135008417</compressibilityFactor>
+            <density>747.936268215431</density>
+            <enthalpy>185.832777551233</enthalpy>
+            <entropy>0.503734436952634</entropy>
+            <heatCapacityCp>0</heatCapacityCp>
+            <heatCapacityCv>0</heatCapacityCv>
+            <kinematic_viscosity>3.12547653408567E-07</kinematic_viscosity>
+            <massflow>0.0481312282239005</massflow>
+            <massfraction>0.999999999999998</massfraction>
+            <molar_enthalpy>11464.6537427478</molar_enthalpy>
+            <molar_entropy>31.0770843231239</molar_entropy>
+            <molarflow>0.78016833552061</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>61.6933885067026</molecularWeight>
+            <thermalConductivity>0.120307882424234</thermalConductivity>
+            <viscosity>0.000233765725529893</viscosity>
+            <volumetric_flow>6.43520447788168E-05</volumetric_flow>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.0659014819911476</helmholtz_energy>
+            <internal_energy>185.766876069242</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-4.06568573164734</molar_helmholtz_energy>
+            <molar_internal_energy>11460.5880570162</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>2</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>4.07917369751543E-13</MassFraction>
+              <MoleFraction>4.71539613410424E-13</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>26.1859358578682</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>5.87219541532721E-11</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.107952609231912</MassFraction>
+              <MoleFraction>0.402307647999366</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>8.12248539736532</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>3.14909481177876E-10</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.89204739076768</MassFraction>
+              <MoleFraction>0.597692352000162</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>45.1777203455511</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>2.65025205694262E-11</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Vapor</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Vapor</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+            <idealGasHeatCapacityCp>1.96382536092348</idealGasHeatCapacityCp>
+            <idealGasHeatCapacityRatio>1.0631930833244</idealGasHeatCapacityRatio>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>3</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>6.52554770166032</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>2.06390062054608E-14</MassFraction>
+              <MoleFraction>2.1923365742429E-14</MoleFraction>
+              <Molarity>2.6578667110063E-10</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>21.5085411141129</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>9.9338071798953E-16</MassFlow>
+              <MolarFlow>1.71039157602804E-14</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>2.22138503385161E-09</PartialPressure>
+              <PartialVolume>-0.0829883956543016</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>1.00008758260384</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.136822840719863</MassFraction>
+              <MoleFraction>0.468550290038299</MoleFraction>
+              <Molarity>5680.44265171834</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0.858622129940072</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.00658545137293009</MassFlow>
+              <MolarFlow>0.365548099886879</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>47475.8581381307</PartialPressure>
+              <PartialVolume>0.0187413369026188</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>1.20788816448314E-08</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>1.00065583232412</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.863177159280117</MassFraction>
+              <MoleFraction>0.531449709961679</MoleFraction>
+              <Molarity>6443.0001728585</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1.12464517492925</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0415457768509694</MassFlow>
+              <MolarFlow>0.414620235633714</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>53849.1418618671</PartialPressure>
+              <PartialVolume>-0.160163998201726</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid1</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid1</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <compressibilityFactor>0.00132557135008417</compressibilityFactor>
+            <density>747.936268215431</density>
+            <enthalpy>185.832777551233</enthalpy>
+            <enthalpyF>-3298.88897377448</enthalpyF>
+            <entropy>0.503734436952634</entropy>
+            <entropyF>0.503734436952307</entropyF>
+            <heatCapacityCp>0</heatCapacityCp>
+            <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+            <kinematic_viscosity>3.12547653408567E-07</kinematic_viscosity>
+            <massflow>0.0481312282239005</massflow>
+            <massfraction>0.999999999999998</massfraction>
+            <molar_enthalpy>11464.6537427478</molar_enthalpy>
+            <molar_entropy>31.0770843231239</molar_entropy>
+            <molarflow>0.78016833552061</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>61.6933885067026</molecularWeight>
+            <speedOfSound>NaN</speedOfSound>
+            <thermalConductivity>0.120307882424234</thermalConductivity>
+            <viscosity>0.000233765725529893</viscosity>
+            <volumetric_flow>6.43520447788168E-05</volumetric_flow>
+            <bulk_modulus>-94.6317497974457</bulk_modulus>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.0659014819911476</helmholtz_energy>
+            <internal_energy>185.766876069242</internal_energy>
+            <isothermal_compressibility>-0.010567277918251</isothermal_compressibility>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-4.06568573164734</molar_helmholtz_energy>
+            <molar_internal_energy>11460.5880570162</molar_internal_energy>
+            <idealGasHeatCapacityCp>1.96166961448807</idealGasHeatCapacityCp>
+            <idealGasHeatCapacityRatio>1.07376580750886</idealGasHeatCapacityRatio>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>4</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0829883956543016</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0187413369026188</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.160163998201726</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid2</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid2</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>5</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0829883956543016</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0187413369026188</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.160163998201726</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>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>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0829883956543016</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0187413369026188</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.160163998201726</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>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>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0829883956543016</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0187413369026188</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.160163998201726</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Solid</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Solid</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+      </Phases>
+    </SimulationObject>
+    <SimulationObject>
+      <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+      <ObjectClass>Streams</ObjectClass>
+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+      <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+      <ComponentName>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</ComponentName>
+      <EnergyFlow>8.93828063257156</EnergyFlow>
+      <MobileCompatible>true</MobileCompatible>
+      <Name2>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name2>
+      <code>0</code>
+      <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>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name>
+      <UserDefinedChartNames />
+      <ProductName>Energy Stream</ProductName>
+      <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <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>Mole</DefinedFlow>
+      <ForcePhase>GlobalDef</ForcePhase>
+      <TotalEnergyFlow>-154.291636193291</TotalEnergyFlow>
+      <AtEquilibrium>true</AtEquilibrium>
+      <ComponentDescription>CorrentedeMatria</ComponentDescription>
+      <ComponentName>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</ComponentName>
+      <Name2>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</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>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name>
+      <UserDefinedChartNames />
+      <ProductName>Material Stream</ProductName>
+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+      <Phases>
+        <Phase>
+          <ID>0</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.353390589738737</MassFraction>
+              <MoleFraction>0.46790357445438</MoleFraction>
+              <Molarity>4312.42913406151</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>1.61258634580789</Kvalue>
+              <lnKvalue>0.477839316041996</lnKvalue>
+              <MassFlow>0.0212014156130144</MassFlow>
+              <MolarFlow>0.365043552866217</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0</PartialVolume>
+              <VolumetricFlow>-0.000158396019674656</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.0102429381170448</MassFraction>
+              <MoleFraction>0.043722510590787</MoleFraction>
+              <Molarity>402.968130144956</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0.291484400663683</Kvalue>
+              <lnKvalue>-1.23276878864176</lnKvalue>
+              <MassFlow>0.000614517744454951</MassFlow>
+              <MolarFlow>0.0341109183123965</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0</PartialVolume>
+              <VolumetricFlow>3.49329705236692E-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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.636366472144218</MassFraction>
+              <MoleFraction>0.48837391495483</MoleFraction>
+              <Molarity>4501.09384529232</Molarity>
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+              <Kvalue>0.47652146799572</Kvalue>
+              <lnKvalue>-0.741242503396525</lnKvalue>
+              <MassFlow>0.0381783512347965</MassFlow>
+              <MolarFlow>0.381013864341994</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0</PartialVolume>
+              <VolumetricFlow>0.000324201065397565</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>708.740364598857</density>
+            <enthalpy>93.2778591049466</enthalpy>
+            <entropy>0.281905762245771</entropy>
+            <heatCapacityCp>0</heatCapacityCp>
+            <heatCapacityCv>0</heatCapacityCv>
+            <massflow>0.0599942845922659</massflow>
+            <molar_enthalpy>7172.98840584848</molar_enthalpy>
+            <molar_entropy>21.6783144846381</molar_entropy>
+            <molarflow>0.78016833552061</molarflow>
+            <molecularWeight>76.8991535041362</molecularWeight>
+            <pressure>101325</pressure>
+            <surfaceTension>0.0197031957424113</surfaceTension>
+            <temperature>330.883123359589</temperature>
+            <thermalConductivity>0.12201792032145</thermalConductivity>
+            <volumetric_flow>8.46491713876383E-05</volumetric_flow>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.124761576248531</helmholtz_energy>
+            <internal_energy>93.1530975286981</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-9.59405960335381</molar_helmholtz_energy>
+            <molar_internal_energy>7163.39434624513</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>1</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.353390589738737</MassFraction>
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+              <Molarity>4312.42913406153</Molarity>
+              <Molality>0</Molality>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0212014156130145</MassFlow>
+              <MolarFlow>0.365043552866219</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0775826295199718</PartialVolume>
+              <VolumetricFlow>-7.91980098373278E-05</VolumetricFlow>
+              <VolumetricFraction>-0.93560289532726</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.0102429381170448</MassFraction>
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+              <Molarity>402.968130144958</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.000614517744454953</MassFlow>
+              <MolarFlow>0.0341109183123966</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183107873823241</PartialVolume>
+              <VolumetricFlow>1.74664852618346E-06</VolumetricFlow>
+              <VolumetricFraction>0.0206339707471553</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.636366472144218</MassFraction>
+              <MoleFraction>0.488373914954831</MoleFraction>
+              <Molarity>4501.09384529234</Molarity>
+              <Molality>0</Molality>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0381783512347966</MassFlow>
+              <MolarFlow>0.381013864341995</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152138304641278</PartialVolume>
+              <VolumetricFlow>0.000162100532698783</VolumetricFlow>
+              <VolumetricFraction>1.9149689245801</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>0.00348752858101998</compressibilityFactor>
+            <density>708.740364598859</density>
+            <enthalpy>93.2778591049463</enthalpy>
+            <entropy>0.281905762245771</entropy>
+            <heatCapacityCp>0</heatCapacityCp>
+            <heatCapacityCv>0</heatCapacityCv>
+            <kinematic_viscosity>3.55602750626295E-07</kinematic_viscosity>
+            <massflow>0.059994284592266</massflow>
+            <massfraction>1</massfraction>
+            <molar_enthalpy>7172.98840584848</molar_enthalpy>
+            <molar_entropy>21.6783144846381</molar_entropy>
+            <molarflow>0.78016833552061</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>76.8991535041365</molecularWeight>
+            <thermalConductivity>0.12201792032145</thermalConductivity>
+            <viscosity>0.000252030023131238</viscosity>
+            <volumetric_flow>8.46491713876383E-05</volumetric_flow>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.124761576248531</helmholtz_energy>
+            <internal_energy>93.1530975286978</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-9.59405960335381</molar_helmholtz_energy>
+            <molar_internal_energy>7163.39434624513</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
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+          <Compounds>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.650464936810833</MassFraction>
+              <MoleFraction>0.75453491531984</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>23.4052117297934</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>4.85422491385702E-11</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.00340789180846115</MassFraction>
+              <MoleFraction>0.0127444297950671</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>7.25994638990027</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>2.60318559078173E-10</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.346127171380706</MassFraction>
+              <MoleFraction>0.232720654885093</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>40.3802299026597</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>2.19081938745304E-11</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Vapor</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Vapor</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>3</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>1.52743555608834</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.353390589738737</MassFraction>
+              <MoleFraction>0.467903574454381</MoleFraction>
+              <Molarity>4312.42913406153</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1.61258638235274</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0212014156130145</MassFlow>
+              <MolarFlow>0.365043552866219</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>47410.3296815902</PartialPressure>
+              <PartialVolume>-0.0775826295199718</PartialVolume>
+              <VolumetricFlow>-7.91980098373278E-05</VolumetricFlow>
+              <VolumetricFraction>-0.93560289532726</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>1.64376537826977</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.0102429381170448</MassFraction>
+              <MoleFraction>0.0437225105907871</MoleFraction>
+              <Molarity>402.968130144958</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0.291484407269379</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.000614517744454953</MassFlow>
+              <MolarFlow>0.0341109183123966</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>4430.18338561151</PartialPressure>
+              <PartialVolume>0.0183107873823241</PartialVolume>
+              <VolumetricFlow>1.74664852618346E-06</VolumetricFlow>
+              <VolumetricFraction>0.0206339707471553</VolumetricFraction>
+              <DiffusionCoefficient>1.01897927557463E-08</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>1.47523255813548</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.636366472144218</MassFraction>
+              <MoleFraction>0.488373914954831</MoleFraction>
+              <Molarity>4501.09384529234</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0.476521478794775</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0381783512347966</MassFlow>
+              <MolarFlow>0.381013864341995</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>49484.4869327983</PartialPressure>
+              <PartialVolume>0.152138304641278</PartialVolume>
+              <VolumetricFlow>0.000162100532698783</VolumetricFlow>
+              <VolumetricFraction>1.9149689245801</VolumetricFraction>
+              <DiffusionCoefficient>6.74627602514587E-09</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid1</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid1</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <compressibilityFactor>0.00348752858101998</compressibilityFactor>
+            <density>708.740364598859</density>
+            <enthalpy>93.2778591049463</enthalpy>
+            <enthalpyF>-2571.77224867153</enthalpyF>
+            <entropy>0.281905762245771</entropy>
+            <entropyF>-5.31057424362785</entropyF>
+            <heatCapacityCp>0</heatCapacityCp>
+            <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+            <kinematic_viscosity>3.55602750626295E-07</kinematic_viscosity>
+            <massflow>0.059994284592266</massflow>
+            <massfraction>1</massfraction>
+            <molar_enthalpy>7172.98840584848</molar_enthalpy>
+            <molar_entropy>21.6783144846381</molar_entropy>
+            <molarflow>0.78016833552061</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>76.8991535041365</molecularWeight>
+            <speedOfSound>NaN</speedOfSound>
+            <thermalConductivity>0.12201792032145</thermalConductivity>
+            <viscosity>0.000252030023131238</viscosity>
+            <volumetric_flow>8.46491713876383E-05</volumetric_flow>
+            <bulk_modulus>-684.702940051689</bulk_modulus>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.124761576248531</helmholtz_energy>
+            <internal_energy>93.1530975286978</internal_energy>
+            <isothermal_compressibility>-0.00146048737562673</isothermal_compressibility>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-9.59405960335381</molar_helmholtz_energy>
+            <molar_internal_energy>7163.39434624513</molar_internal_energy>
+            <idealGasHeatCapacityCp>1.64827638256005</idealGasHeatCapacityCp>
+            <idealGasHeatCapacityRatio>1.07019762311817</idealGasHeatCapacityRatio>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>4</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0775826295199718</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183107873823241</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152138304641278</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid2</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid2</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>5</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0775826295199718</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183107873823241</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152138304641278</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>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0775826295199718</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183107873823241</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152138304641278</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>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0775826295199718</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183107873823241</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152138304641278</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Solid</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Solid</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+      </Phases>
+    </SimulationObject>
+    <SimulationObject>
+      <Type>DWSIM.UnitOperations.UnitOperations.CapeOpenUO</Type>
+      <ObjectClass>CAPEOPEN</ObjectClass>
+      <EmbeddedImageData></EmbeddedImageData>
+      <UseEmbeddedImage>false</UseEmbeddedImage>
+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+      <ReactionSetID>DefaultSet</ReactionSetID>
+      <ReactionSetName></ReactionSetName>
+      <RecalcOutputStreams>true</RecalcOutputStreams>
+      <MobileCompatible>false</MobileCompatible>
+      <ProductName>ChemSep Column / Flash</ProductName>
+      <ProductDescription>ChemSep CAPE-OPEN Unit Operation</ProductDescription>
+      <ProductAuthor>Copyright (C) Ross Taylor and Harry Kooijman 2020</ProductAuthor>
+      <ProductContactInfo></ProductContactInfo>
+      <ProductPage>http://www.chemsep.com/</ProductPage>
+      <ProductVersion>2.0.0.10</ProductVersion>
+      <ProductAssembly>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</ProductAssembly>
+      <ExternalSolverID></ExternalSolverID>
+      <ExternalSolverConfigData></ExternalSolverConfigData>
+      <ComponentDescription>CapeOpenUnitOperation</ComponentDescription>
+      <ComponentName>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</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>11/12/2023 02:00:30</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</Name>
+      <UserDefinedChartNames />
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+      <CAPEOPEN_Object_Info>
+        <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.CapeOpen.CapeOpenUnitOpInfo</Type>
+        <TypeName>ChemSepUO.ChemSep_UnitOperation.1</TypeName>
+        <Version>2.0.0.10</Version>
+        <Description>ChemSep CAPE-OPEN Unit Operation</Description>
+        <HelpURL></HelpURL>
+        <VendorURL>http://www.chemsep.com/</VendorURL>
+        <AboutInfo>Copyright (C) Ross Taylor and Harry Kooijman 2020</AboutInfo>
+        <CapeVersion>1.0</CapeVersion>
+        <Location>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</Location>
+        <Name>ChemSep Column / Flash</Name>
+        <ImplementedCategory></ImplementedCategory>
+      </CAPEOPEN_Object_Info>
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+    </SimulationObject>
+    <SimulationObject>
+      <Type>DWSIM.UnitOperations.UnitOperations.CapeOpenUO</Type>
+      <ObjectClass>CAPEOPEN</ObjectClass>
+      <EmbeddedImageData></EmbeddedImageData>
+      <UseEmbeddedImage>false</UseEmbeddedImage>
+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+      <ReactionSetID>DefaultSet</ReactionSetID>
+      <ReactionSetName></ReactionSetName>
+      <RecalcOutputStreams>true</RecalcOutputStreams>
+      <MobileCompatible>false</MobileCompatible>
+      <ProductName>ChemSep Column / Flash</ProductName>
+      <ProductDescription>ChemSep CAPE-OPEN Unit Operation</ProductDescription>
+      <ProductAuthor>Copyright (C) Ross Taylor and Harry Kooijman 2020</ProductAuthor>
+      <ProductContactInfo></ProductContactInfo>
+      <ProductPage>http://www.chemsep.com/</ProductPage>
+      <ProductVersion>2.0.0.10</ProductVersion>
+      <ProductAssembly>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</ProductAssembly>
+      <ExternalSolverID></ExternalSolverID>
+      <ExternalSolverConfigData></ExternalSolverConfigData>
+      <ComponentDescription>CapeOpenUnitOperation</ComponentDescription>
+      <ComponentName>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</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>11/12/2023 02:00:26</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</Name>
+      <UserDefinedChartNames />
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+      <CAPEOPEN_Object_Info>
+        <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.CapeOpen.CapeOpenUnitOpInfo</Type>
+        <TypeName>ChemSepUO.ChemSep_UnitOperation.1</TypeName>
+        <Version>2.0.0.10</Version>
+        <Description>ChemSep CAPE-OPEN Unit Operation</Description>
+        <HelpURL></HelpURL>
+        <VendorURL>http://www.chemsep.com/</VendorURL>
+        <AboutInfo>Copyright (C) Ross Taylor and Harry Kooijman 2020</AboutInfo>
+        <CapeVersion>1.0</CapeVersion>
+        <Location>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</Location>
+        <Name>ChemSep Column / Flash</Name>
+        <ImplementedCategory></ImplementedCategory>
+      </CAPEOPEN_Object_Info>
+      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wBMAC0AMQAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAEMAYQBwAGUALQBPAHAAZQBuACAAdQBuAGkAdAAgAGkAZAA6ACAAQwBTAF8ANABfADYANwBCADQAXwAxAEQAQQAxADQARABBAF8ARABCADgANAAyAEUAQgAwACAAIAAgACAAIAAgAA0ACgBDAGEAcABlAC0ATwBwAGUAbgAgAHIAdQBuACAAbABlAHYAZQBsADoAIABuAG8AcgBtAGEAbAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgAA0ACgBDAGEAcABlAC0ATwBwAGUAbgAgAEkAbgBpAHQAaQBhAGwAaQB6AGUAZAANAAoAQwBhAHAAZQAtAE8AcABlAG4AIABUAGgAZQByAG0AbwBkAHkAbgBhAG0AaQBjAC0AcAByAG8AcABlAHIAdABpAGUAcwAgAGQAaQBzAGEAYgBsAGUAZAANAAoAUgBlAGEAZABpAG4AZwAgAGMAbwBuAGYAaQBnAHUAcgBhAHQAaQBvAG4ADQAKAFIAZQBhAGQAaQBuAGcAIABjAG8AbQBwAG8AbgBlAG4AdAAgAHAAcgBvAHAAZQByAHQAeQAgAGwAaQBiAHIAYQByAGkAZQBzAA0ACgBSAGUAYQBkAGkAbgBnACAAdABoAGUAcgBtAG8AZAB5AG4AYQBtAGkAYwAgAHAAcgBvAHAAZQByAHQAeQAgAG8AcAB0AGkAbwBuAHMADQAKAEsALQB2AGEAbAB1AGUAOgAgAEQARQBDAEgARQBNAEEADQAKAFIAZQBhAGQAaQBuAGcAIABwAGgAeQBzAGkAYwBhAGwAIABwAHIAbwBwAGUAcgB0AHkAIABvAHAAdABpAG8AbgBzAA0ACgBSAGUAYQBkAGkAbgBnACAAdABoAGUAcgBtAG8AZAB5AG4AYQBtAGkAYwAgAHAAcgBvAHAAZQByAHQAeQAgAGQAYQB0AGEADQAKAFcAYQByAG4AaQBuAGcAIQAhACAARQBzAHQAaQBtAGEAdABpAG4AZwAgAGEAYwB0AGkAdgBpAHQAeQAgAG0AbwBkAGUAbAAgAHAAYQByAGEAbQBlAHQAZQByAHMADQAKAFIAZQBhAGQAaQBuAGcAIAByAGUAYQBjAHQAaQBvAG4AIABkAGEAdABhAA0ACgBSAGUAYQBkAGkAbgBnACAAcwBwAGUAYwBpAGYAaQBjAGEAdABpAG8AbgBzAA0ACgBDAGgAZQBjAGsAaQBuAGcAIABjAG8AbQBwAG8AbgBlAG4AdABzACAAZABhAHQAYQAgACgAMwApAA0ACgBEAGUAdABlAHIAbQBpAG4AaQBuAGcAIABmAGUAZQBkACAAYwBvAG4AZABpAHQAaQBvAG4AcwANAAoAIABGAGUAZQBkAC0AZgBsAGEAcwBoACAAbwBuACAAcwB0AGEAZwBlACAAIAA0AA0ACgAgAEYAZQBlAGQALQBmAGwAYQBzAGgAIABvAG4AIABzAHQAYQBnAGUAIAAxADYADQAKAFIAZQBhAGQAaQBuAGcAIAAgACAAIAAgACAAIAA0ADQAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAUgB1AG4AIABsAGUAdgBlAGwAOgAgAEkAbgBpAHQAaQBhAGwAaQB6AGEAdABpAG8AbgAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAFIAZQBhAGQAaQBuAGcAIABpAG4AaQB0AGkAYQBsACAAdABlAG0AcABlAHIAYQB0AHUAcgBlACAAcAByAG8AZgBpAGwAZQBzAA0ACgBJAG4AaQB0AGkAYQBsAGkAegBpAG4AZwAgAGYAcgBvAG0AIABvAGwAZAAgAHIAZQBzAHUAbAB0AHMADQAKAFIAZQBhAGQAaQBuAGcAIABpAG4AaQB0AGkAYQBsACAAYwBvAG0AcABvAHMAaQB0AGkAbwBuACAAcAByAG8AZgBpAGwAZQBzAA0ACgBJAG4AaQB0AGkAYQBsAGkAegBhAHQAaQBvAG4AIAAgACAAIAAgACAAIAAgADAAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAUgB1AG4AIABsAGUAdgBlAGwAOgAgAEMAbwBtAHAAbABlAHQAZQAgAG0AbwBkAGUAbAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgAA0ACgANAAoAIAAgACAAIAAgACAASQB0AGUAcgBhAHQAaQBvAG4AIAAgACAAIABsAG8AZwAoAEUAcgByAC8AVABvAGwAKQANAAoAIAAgACAAIAAgACAAIAAgACAAMAAgACAAIAAgACAAIAAgACAAIAAgACAAMgAuADYANgAyADIADQAKACAAIAAgACAAIAAgACAAIAAgADEAIAAgACAAIAAgACAAIAAgACAAIAAgADMALgA3ADcAMAA1AA0ACgAgACAAIAAgACAAIAAgACAAIAAyACAAIAAgACAAIAAgACAAIAAgACAAIAAxAC4AOAA4ADMAMwANAAoAIAAgACAAIAAgACAAIAAgACAAMwAgACAAIAAgACAAIAAgACAAIAAgAC0AMQAuADkANAA1ADcADQAKAFMAaQBtAHUAbABhAHQAaQBvAG4AIAAgACAAIAAgACAAIAA0ADAAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAUgB1AG4AIABsAGUAdgBlAGwAOgAgAFIAZQBwAG8AcgB0ACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAEMAbwBuAHYAZQByAGcAZQBuAGMAZQAgAG8AYgB0AGEAaQBuAGUAZAAgAGkAbgAgADMAIABpAHQAZQByAGEAdABpAG8AbgBzACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAFIAZQBwAG8AcgB0ACAAIAAgACAAIAAgACAAIAA5ACAAbQBpAGwAbABpAHMAZQBjAG8AbgBkAHMADQAKAEMAYQBwAGUALQBPAHAAZQBuACAAYwBsAGUAYQBuAHUAcAAgAGMAYQBsAGwAZQBkACAAdwBpAHQAaAAgAGMAbwBuAHYAZQByAGcAZQBkAA0ACgAgAEYAaQB4AE0AZQBtACAAZAByAGkAdgBlAHIAIABkAG8AbgBlAA0ACgANAAoAcgB1AG4AIAB0AGkAbQBlADoAIAAwAC4AMQA2ACAAcwBlAGMAbwBuAGQAcwANAAoAAADjAAAAVQBzAGkAbgBnADoAIABDADoAXABQAHIAbwBnAHIAYQBtACAARgBpAGwAZQBzAFwAQwBoAGUAbQBTAGUAcABMADgAdgA0ADAAXABiAGkAbgBcAGMAbwAtAGMAbwBsADIALgBlAHgAZQANAAoADQAKAEMAQQBQAEUALQBPAFAARQBOACAAdABoAGUAcgBtAG8ALQBwAHIAbwBwAGUAcgB0AGkAZQBzACAAdwBlAHIAZQAgAGQAaQBzAGEAYgBsAGUAZAAuAA0ACgBBAGwAbAAgAGMAYQBsAGMAdQBsAGEAdABpAG8AbgAgAG0AZQB0AGgAbwBkAHMAIABoAGEAdgBlACAAYgBlAGUAbgAgAGQAZQB0AGUAcgBtAGkAbgBlAGQAIABiAHkAIABDAGgAZQBtAFMAZQBwAC4ADQAKAFMAZQBlACAAbwB1AHQAcAB1AHQAIAByAGUAcABvAHIAdAAgAG8AcgAgAGcAcgBhAHAAaABpAGMAYQBsACAAdQBzAGUAcgAgAGkAbgB0AGUAcgBmAGEAYwBlACAAZgBvAHIAIABtAG8AcgBlACAAaQBuAGYAbwByAG0AYQB0AGkAbwBuAC4ADQAKAAAAAAAAAAAAAAAAAAAAAgAAABAAAAAAAKYCDQAAAEYAZQBlAGQAMQBfAHMAdABhAGcAZQAxADYABQAAAEYAZQBlAGQAMQAEAAAAZQBuAAwAA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+      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</ParameterData>
+    </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>-231.96284514096</TotalEnergyFlow>
+      <AtEquilibrium>true</AtEquilibrium>
+      <ComponentDescription>CorrentedeMatria</ComponentDescription>
+      <ComponentName>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</ComponentName>
+      <Name2>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name2>
+      <code>0</code>
+      <InputComposition />
+      <IsElectrolyteStream>false</IsElectrolyteStream>
+      <ReferenceSolvent></ReferenceSolvent>
+      <SpecType>Pressure_and_Enthalpy</SpecType>
+      <CompositionBasis>Molar_Fractions</CompositionBasis>
+      <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"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>11/12/2023 02:00:22</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
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+            <helmholtz_energy>-0.0671007250710113</helmholtz_energy>
+            <internal_energy>0.069903110248216</internal_energy>
+            <isothermal_compressibility>-0.0100596084236128</isothermal_compressibility>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-5.11996937820588</molar_helmholtz_energy>
+            <molar_internal_energy>5.33379905408556</molar_internal_energy>
+            <idealGasHeatCapacityCp>1.64867209641396</idealGasHeatCapacityCp>
+            <idealGasHeatCapacityRatio>1.07076696077004</idealGasHeatCapacityRatio>
+          </Properties>
+        </Phase>
+        <Phase>
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+          <Compounds>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
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+              <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>Acetone</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0737985308993798</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>Water</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>Water</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.018080959744143</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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+              <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>3-methylhexane</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.146373071297317</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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+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
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+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid2</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
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+            <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>
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+              <Molarity>0</Molarity>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+              <PetroleumFraction>false</PetroleumFraction>
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+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
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+              <PartialPressure>0</PartialPressure>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+            <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>
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+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
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+              <PartialVolume>0.0737985308993798</PartialVolume>
+              <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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+              <ComponentName>Water</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>Water</Name>
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+              <PartialVolume>0.018080959744143</PartialVolume>
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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>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
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+              <Molarity>0</Molarity>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146373071297317</PartialVolume>
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+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <MassFlow>0</MassFlow>
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+              <Name>Water</Name>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
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+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
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+              <PartialVolume>0</PartialVolume>
+              <VolumetricFlow>2.13514913383788E-05</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>3-methylhexane</ComponentName>
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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>
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+            <molarflow>1.5603366710412</molarflow>
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+            <pressure>101325</pressure>
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+            <helmholtz_energy>-0.079003966941925</helmholtz_energy>
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+            <molar_helmholtz_energy>-5.47468030134069</molar_helmholtz_energy>
+            <molar_internal_energy>7457.35522015844</molar_internal_energy>
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+              <VolumetricFlow>-4.14707307559925E-05</VolumetricFlow>
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+              <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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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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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>
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+          <Name>OverallLiquid</Name>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <lnKvalue>0</lnKvalue>
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+              <Name>Water</Name>
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
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+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+          </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>
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+            <helmholtz_energy>0</helmholtz_energy>
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+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+              <VolumetricFraction>-0.28359662379612</VolumetricFraction>
+              <DiffusionCoefficient>NaN</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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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+            <idealGasHeatCapacityRatio>1.07444668768553</idealGasHeatCapacityRatio>
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+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
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+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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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>
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+              <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>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152775818520635</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid2</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid2</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>5</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0780058205985097</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183416589386652</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152775818520635</PartialVolume>
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+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+          <Name>Liquid3</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <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>
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+          <ID>6</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>-0.0780058205985097</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183416589386652</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.152775818520635</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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+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Aqueous</ComponentName>
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+          <Name>Aqueous</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <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>
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+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
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+              <PartialVolume>-0.0780058205985097</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>NaN</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+              <ComponentName>Water</ComponentName>
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+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
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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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0183416589386652</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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+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
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+              <Molarity>0</Molarity>
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+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
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+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
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+          <Name>Solid</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
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+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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+            <helmholtz_energy>0</helmholtz_energy>
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+        </Phase>
+      </Phases>
+    </SimulationObject>
+    <SimulationObject>
+      <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
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+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
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+      <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+      <DefinedFlow>Mole</DefinedFlow>
+      <ForcePhase>GlobalDef</ForcePhase>
+      <TotalEnergyFlow>-71.6632443919596</TotalEnergyFlow>
+      <AtEquilibrium>true</AtEquilibrium>
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+      <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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+      <Calculated>true</Calculated>
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+      <LastUpdated>11/12/2023 02:00:30</LastUpdated>
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+      <IsSpecAttached>false</IsSpecAttached>
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+      <Name>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name>
+      <UserDefinedChartNames />
+      <ProductName>Material Stream</ProductName>
+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
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+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
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+            <enthalpy>-51.6540322281299</enthalpy>
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+            <pressure>101325</pressure>
+            <surfaceTension>0.0735289994526015</surfaceTension>
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+            <molar_helmholtz_energy>-2.10151285367827</molar_helmholtz_energy>
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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>Water</ComponentName>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
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+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+          <ComponentName>OverallLiquid</ComponentName>
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+          <Name>OverallLiquid</Name>
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+            <molar_helmholtz_energy>-2.10151285367827</molar_helmholtz_energy>
+            <molar_internal_energy>-975.116121408485</molar_internal_energy>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Vapor</ComponentName>
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+          <Name>Vapor</Name>
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+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+            <idealGasHeatCapacityCp>1.84749766545925</idealGasHeatCapacityCp>
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+              <lnKvalue>0</lnKvalue>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+              <lnKvalue>0</lnKvalue>
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+              <Name>Water</Name>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
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+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+              <MassFlow>0</MassFlow>
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+              <Name>Acetone</Name>
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+              <PartialVolume>0.0724941596865831</PartialVolume>
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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>Water</ComponentName>
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+              <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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180308538169985</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.144359935789163</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>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0724941596865831</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>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180308538169985</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.144359935789163</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>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0724941596865831</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180308538169985</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.144359935789163</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Solid</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Solid</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+      </Phases>
+    </SimulationObject>
+    <SimulationObject>
+      <Type>DWSIM.UnitOperations.UnitOperations.Mixer</Type>
+      <ObjectClass>MixersSplitters</ObjectClass>
+      <SupportsDynamicMode>true</SupportsDynamicMode>
+      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+      <PressureCalculation>Minimum</PressureCalculation>
+      <MobileCompatible>true</MobileCompatible>
+      <ExternalSolverID></ExternalSolverID>
+      <ExternalSolverConfigData></ExternalSolverConfigData>
+      <ComponentDescription>Misturador</ComponentDescription>
+      <ComponentName>MIST-ae80e666-b984-4270-b427-05f406124fe0</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>11/12/2023 02:00:22</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>MIST-ae80e666-b984-4270-b427-05f406124fe0</Name>
+      <UserDefinedChartNames />
+      <ProductName>Stream Mixer</ProductName>
+      <ProductDescription>Mixes multiple Material Streams into a single one</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</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>Mass</DefinedFlow>
+      <ForcePhase>GlobalDef</ForcePhase>
+      <TotalEnergyFlow>-166.710668180743</TotalEnergyFlow>
+      <AtEquilibrium>true</AtEquilibrium>
+      <ComponentDescription>CorrentedeMatria</ComponentDescription>
+      <ComponentName>MAT-9f510731-7729-4083-8c48-1c157b4ee026</ComponentName>
+      <Name2>MAT-9f510731-7729-4083-8c48-1c157b4ee026</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>11/12/2023 02:00:22</LastUpdated>
+      <Annotation></Annotation>
+      <IsAdjustAttached>false</IsAdjustAttached>
+      <AttachedAdjustId></AttachedAdjustId>
+      <AdjustVarType>Manipulated</AdjustVarType>
+      <IsSpecAttached>false</IsSpecAttached>
+      <AttachedSpecId></AttachedSpecId>
+      <SpecVarType>Source</SpecVarType>
+      <Name>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name>
+      <UserDefinedChartNames />
+      <ProductName>Material Stream</ProductName>
+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+      <ProductVersion>8.6.5.0</ProductVersion>
+      <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+      <IsSource>false</IsSource>
+      <IsSink>false</IsSink>
+      <DynamicProperties />
+      <DynamicPropertiesDescriptions />
+      <DynamicPropertiesUnitTypes />
+      <AttachedUtilities />
+      <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+      <Phases>
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+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.763250971621835</MassFraction>
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+              <Molarity>11556.5422306546</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>1.79548461964337</Kvalue>
+              <lnKvalue>0.585274968589596</lnKvalue>
+              <MassFlow>0.0212014158783843</MassFlow>
+              <MolarFlow>0.365043557435325</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0</PartialVolume>
+              <VolumetricFlow>5.07429608938772E-05</VolumetricFlow>
+              <VolumetricFraction>1.60641972316535</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0.236749028378165</MassFraction>
+              <MoleFraction>0.5</MoleFraction>
+              <Molarity>11556.5422306546</Molarity>
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+              <FugacityCoeff>0</FugacityCoeff>
+              <Kvalue>0.204515380356629</Kvalue>
+              <lnKvalue>-1.58711209675951</lnKvalue>
+              <MassFlow>0.00657636189939347</MassFlow>
+              <MolarFlow>0.365043557435325</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0</PartialVolume>
+              <VolumetricFlow>1.24322605779949E-05</VolumetricFlow>
+              <VolumetricFraction>0.393580276834651</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>3-methylhexane</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>3-methylhexane</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>879.388378247172</density>
+            <enthalpy>10.867318406018</enthalpy>
+            <entropy>0.0364491645346906</entropy>
+            <heatCapacityCp>0</heatCapacityCp>
+            <heatCapacityCv>0</heatCapacityCv>
+            <massflow>0.0277777777777778</massflow>
+            <molar_enthalpy>413.471145530632</molar_enthalpy>
+            <molar_entropy>1.38678901737593</molar_entropy>
+            <molarflow>0.730087114870651</molarflow>
+            <molecularWeight>38.04721</molecularWeight>
+            <pressure>101325</pressure>
+            <surfaceTension>0.0475505128088451</surfaceTension>
+            <temperature>298.15</temperature>
+            <thermalConductivity>0.211684674125455</thermalConductivity>
+            <volumetric_flow>3.15876107359361E-05</volumetric_flow>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.085641233109552</helmholtz_energy>
+            <internal_energy>10.7816771729085</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
+            <molar_internal_energy>410.212735549854</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>1</ID>
+          <Compounds>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
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+              <MassFlow>0.0212014158783843</MassFlow>
+              <MolarFlow>0.365043557435325</MolarFlow>
+              <Name>Acetone</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>Water</ComponentName>
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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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+              <MolarFlow>0</MolarFlow>
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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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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
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+              <PetroleumFraction>false</PetroleumFraction>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+          <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>
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+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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+            <helmholtz_energy>0</helmholtz_energy>
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+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+              <ComponentDescription></ComponentDescription>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <Name>3-methylhexane</Name>
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+            <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
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+            <speedOfSound>NaN</speedOfSound>
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+            <idealGasHeatCapacityRatio>1.18132337598044</idealGasHeatCapacityRatio>
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+              <Molarity>0</Molarity>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+              <FugacityCoeff>NaN</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
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+              <VolumetricFlow>0</VolumetricFlow>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <PetroleumFraction>false</PetroleumFraction>
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+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>NaN</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+              <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>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
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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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+            <molarflow>0.78016833552061</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>61.6933885067027</molecularWeight>
+            <thermalConductivity>0.139308428645295</thermalConductivity>
+            <viscosity>0.000605165484337862</viscosity>
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+            <internal_energy>0.0661337504746934</internal_energy>
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+            <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
+            <molar_internal_energy>4.08001516144059</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>2</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
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+              <lnKvalue>0</lnKvalue>
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+              <MolarFlow>0</MolarFlow>
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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>Water</ComponentName>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</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>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
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+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+        </Phase>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <MassFlow>9.93380717989532E-16</MassFlow>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
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+          <Name>Liquid1</Name>
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+            <entropyF>0.000423627682931141</entropyF>
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+            <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+            <kinematic_viscosity>7.54356581787694E-07</kinematic_viscosity>
+            <massflow>0.0481312282239006</massflow>
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+            <molecularWeight>61.6933885067027</molecularWeight>
+            <speedOfSound>NaN</speedOfSound>
+            <thermalConductivity>0.139308428645295</thermalConductivity>
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+            <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
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+            <idealGasHeatCapacityRatio>1.08808958782905</idealGasHeatCapacityRatio>
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+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>NaN</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0737984191993252</PartialVolume>
+              <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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+              <FugacityCoeff>NaN</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0180809547091451</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
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+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
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+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
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+          <ComponentDescription></ComponentDescription>
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+          <Name>Liquid2</Name>
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+            <helmholtz_energy>0</helmholtz_energy>
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+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <ComponentName>Acetone</ComponentName>
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+              <lnKvalue>0</lnKvalue>
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+              <Name>Acetone</Name>
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+              <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>Water</ComponentName>
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+              <PetroleumFraction>false</PetroleumFraction>
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+              <Name>Water</Name>
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+              <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>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
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+              <PetroleumFraction>false</PetroleumFraction>
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+              <Molality>0</Molality>
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+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</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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+          <Name>Liquid3</Name>
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+            <helmholtz_energy>0</helmholtz_energy>
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+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
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+        <Phase>
+          <ID>6</ID>
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+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+              <ComponentName>Acetone</ComponentName>
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+              <PetroleumFraction>false</PetroleumFraction>
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+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
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+              <PartialVolume>0.0737984191993252</PartialVolume>
+              <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>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
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+              <Molarity>0</Molarity>
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+              <MassFlow>0</MassFlow>
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+              <PartialVolume>0.0180809547091451</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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+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
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+      <ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
+      <ProductAuthor>Daniel Medeiros</ProductAuthor>
+      <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+      <ProductPage>https://dwsim.inforside.com.br</ProductPage>
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+              <Name>3-methylhexane</Name>
+              <PartialPressure>101325</PartialPressure>
+              <PartialVolume>24.4640424377005</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Vapor</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Vapor</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>3</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</ComponentName>
+              <ActivityCoeff>7.17641923898794</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>2.17188219124978</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0737984191993252</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>5.18354190784942E-09</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Water</ComponentName>
+              <ActivityCoeff>1.00071619041225</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0.0313434094895189</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>6.71324433876425E-09</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>3-methylhexane</ComponentName>
+              <ActivityCoeff>1.00551404572158</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>1</MassFraction>
+              <MoleFraction>1</MoleFraction>
+              <Molarity>6832.55660172031</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>0.0813875285498942</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0.0416666666666667</MassFlow>
+              <MolarFlow>0.415826696739253</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>101325</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>6.08596051197813E-05</VolumetricFlow>
+              <VolumetricFraction>1</VolumetricFraction>
+              <DiffusionCoefficient>4.51446770417322E-09</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid1</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid1</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <compressibilityFactor>0.00598235873487061</compressibilityFactor>
+            <density>684.635836605579</density>
+            <enthalpy>0.147998387730284</enthalpy>
+            <enthalpyF>-1909.29492690318</enthalpyF>
+            <entropy>0.000496389024753595</entropy>
+            <entropyF>0.000496389024753595</entropyF>
+            <heatCapacityCp>0</heatCapacityCp>
+            <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+            <kinematic_viscosity>5.07314344208017E-07</kinematic_viscosity>
+            <massflow>0.0416666666666667</massflow>
+            <massfraction>1</massfraction>
+            <molar_enthalpy>14.8297344473499</molar_enthalpy>
+            <molar_entropy>0.0497391730583597</molar_entropy>
+            <molarflow>0.415826696739253</molarflow>
+            <molarfraction>1</molarfraction>
+            <molecularWeight>100.202</molecularWeight>
+            <speedOfSound>NaN</speedOfSound>
+            <thermalConductivity>0.118010205685203</thermalConductivity>
+            <viscosity>0.000347325580468866</viscosity>
+            <volumetric_flow>6.08596051197813E-05</volumetric_flow>
+            <bulk_modulus>-2709104.05471673</bulk_modulus>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>-0.147992905281822</helmholtz_energy>
+            <internal_energy>5.4824484624072E-06</internal_energy>
+            <isothermal_compressibility>-3.69125725628343E-07</isothermal_compressibility>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
+            <molar_internal_energy>0.000549352300830126</molar_internal_energy>
+            <idealGasHeatCapacityCp>1.63261361609135</idealGasHeatCapacityCp>
+            <idealGasHeatCapacityRatio>1.05354297154205</idealGasHeatCapacityRatio>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>4</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>Water</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>Water</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>NaN</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Liquid2</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Liquid2</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+        <Phase>
+          <ID>5</ID>
+          <Compounds>
+            <Compound>
+              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+              <ComponentDescription></ComponentDescription>
+              <ComponentName>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</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>Acetone</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>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>Water</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>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</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>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</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>Acetone</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Acetone</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0737984191993252</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>Water</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>0</MassFraction>
+              <MoleFraction>0</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>Water</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.0180809547091451</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>3-methylhexane</ComponentName>
+              <ActivityCoeff>0</ActivityCoeff>
+              <PetroleumFraction>false</PetroleumFraction>
+              <MassFraction>1</MassFraction>
+              <MoleFraction>1</MoleFraction>
+              <Molarity>0</Molarity>
+              <Molality>0</Molality>
+              <FugacityCoeff>1</FugacityCoeff>
+              <Kvalue>0</Kvalue>
+              <lnKvalue>0</lnKvalue>
+              <MassFlow>0</MassFlow>
+              <MolarFlow>0</MolarFlow>
+              <Name>3-methylhexane</Name>
+              <PartialPressure>0</PartialPressure>
+              <PartialVolume>0.146372899520274</PartialVolume>
+              <VolumetricFlow>0</VolumetricFlow>
+              <VolumetricFraction>0</VolumetricFraction>
+              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+              <EntropyF_Dmol>0</EntropyF_Dmol>
+              <DynamicProperties />
+            </Compound>
+          </Compounds>
+          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+          <ComponentDescription></ComponentDescription>
+          <ComponentName>Solid</ComponentName>
+          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+          <Name>Solid</Name>
+          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+          <Properties>
+            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+            <gibbs_free_energy>0</gibbs_free_energy>
+            <helmholtz_energy>0</helmholtz_energy>
+            <internal_energy>0</internal_energy>
+            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+            <molar_helmholtz_energy>0</molar_helmholtz_energy>
+            <molar_internal_energy>0</molar_internal_energy>
+          </Properties>
+        </Phase>
+      </Phases>
+    </SimulationObject>
+  </SimulationObjects>
+  <Settings>
+    <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables</Type>
+    <SelectedPropertyPackage>
+      <Type>DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage</Type>
+      <ComponentName>NRTL</ComponentName>
+      <ComponentDescription>Uses NRTL (Non-Random Two-Liquid) model to calculate liquid-phase activity coefficients.</ComponentDescription>
+      <Tag>NRTL (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>LiqCp_Excess</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>
+      <ForcedSolids>[]</ForcedSolids>
+      <PropertyOverrides>{}</PropertyOverrides>
+      <InteractionParameters_PR />
+      <InteractionParameters_NRTL>
+        <InteractionParameter Compound1="Acetone" Compound2="3-methylhexane" ID1="" ID2="" A12="292.355969237514" A21="901.544671308057" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
+        <InteractionParameter Compound1="Water" Compound2="Acetone" ID1="1921" ID2="1051" A12="1324.9767" A21="814.1435" B12="0" B21="0" C12="0" C21="0" alpha12="0.5663" />
+        <InteractionParameter Compound1="Water" Compound2="3-methylhexane" ID1="" ID2="" A12="1E-10" A21="1E-10" B12="0" B21="0" C12="0" C21="0" alpha12="1E-10" />
+      </InteractionParameters_NRTL>
+      <FlashSettings>
+        <Setting Name="Replace_PTFlash" Value="False" />
+        <Setting Name="ValidateEquilibriumCalc" Value="False" />
+        <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
+        <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
+        <Setting Name="ValidationGibbsTolerance" Value="0.01" />
+        <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+        <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+        <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+        <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+        <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="NL_FastMode" Value="True" />
+        <Setting Name="IO_FastMode" Value="True" />
+        <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
+        <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
+        <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
+        <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
+        <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
+        <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
+        <Setting Name="ST_Number_of_Random_Tries" Value="20" />
+        <Setting Name="CheckIncipientLiquidForStability" Value="False" />
+        <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
+        <Setting Name="PTFlash_DampingFactor" Value="1.0" />
+        <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
+        <Setting Name="ImmiscibleWaterOption" Value="False" />
+        <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
+        <Setting Name="UseIOFlash" Value="False" />
+        <Setting Name="GibbsMinimizationExternalSolver" Value="" />
+        <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
+        <Setting Name="PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases" Value="False" />
+        <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
+        <Setting Name="FailSafeCalculationMode" Value="1" />
+      </FlashSettings>
+    </SelectedPropertyPackage>
+    <SimulationMode></SimulationMode>
+    <BackupFileName>86822447.dwbcs</BackupFileName>
+    <FilePath>C:\Users\prati\OneDrive\Documents\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>66FBB626BBBAA957C066C6EF837D6E27383E68E8</Key>
+    <NumberFormat>G6</NumberFormat>
+    <Password></Password>
+    <SimulationAuthor>PR80\prati</SimulationAuthor>
+    <SimulationComments></SimulationComments>
+    <SimulationName>MySimulation_6</SimulationName>
+    <UsePassword>false</UsePassword>
+    <SelectedUnitSystem1>
+      <Type>DWSIM.SharedClasses.SystemsOfUnits.SIUnits_Custom5</Type>
+      <accel>m/s2</accel>
+      <activity>Pa</activity>
+      <activityCoefficient>-</activityCoefficient>
+      <area>m2</area>
+      <cakeresistance>m/kg</cakeresistance>
+      <cinematic_viscosity>m2/s</cinematic_viscosity>
+      <compressibility>1/Pa</compressibility>
+      <compressibilityfactor>-</compressibilityfactor>
+      <deltaP>bar</deltaP>
+      <deltaT>C.</deltaT>
+      <density>kg/m3</density>
+      <diameter>mm</diameter>
+      <distance>m</distance>
+      <enthalpy>kJ/kg</enthalpy>
+      <entropy>kJ/[kg.K]</entropy>
+      <excessEnthalpy>kJ/kg</excessEnthalpy>
+      <excessEntropy>kJ/[kg.K]</excessEntropy>
+      <force>N</force>
+      <foulingfactor>K.m2/W</foulingfactor>
+      <fugacity>Pa</fugacity>
+      <fugacityCoefficient>-</fugacityCoefficient>
+      <gor>m3/m3</gor>
+      <head>m</head>
+      <heat_transf_coeff>W/[m2.K]</heat_transf_coeff>
+      <heatCapacityCp>kJ/[kg.K]</heatCapacityCp>
+      <heatCapacityCv>kJ/[kg.K]</heatCapacityCv>
+      <heatflow>kW</heatflow>
+      <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>kmol/m3</molar_conc>
+      <molar_enthalpy>kJ/kmol</molar_enthalpy>
+      <molar_entropy>kJ/[kmol.K]</molar_entropy>
+      <molar_volume>m3/kmol</molar_volume>
+      <molarflow>kmol/h</molarflow>
+      <molarfraction>-</molarfraction>
+      <molecularWeight>kg/kmol</molecularWeight>
+      <Name>C5</Name>
+      <pdp_boilingPointTemperature>C</pdp_boilingPointTemperature>
+      <pdp_meltingTemperature>C</pdp_meltingTemperature>
+      <pressure>bar</pressure>
+      <reac_rate>kmol/[m3.h]</reac_rate>
+      <reac_rate_heterog>kmol/[kg.s]</reac_rate_heterog>
+      <spec_vol>m3/kg</spec_vol>
+      <speedOfSound>m/s</speedOfSound>
+      <surfaceTension>N/m</surfaceTension>
+      <temperature>C</temperature>
+      <thermalConductivity>W/[m.K]</thermalConductivity>
+      <thermalConductivityOfLiquid>W/[m.K]</thermalConductivityOfLiquid>
+      <thermalConductivityOfVapor>W/[m.K]</thermalConductivityOfVapor>
+      <thickness>mm</thickness>
+      <time>h</time>
+      <vaporPressure>bar</vaporPressure>
+      <velocity>m/s</velocity>
+      <viscosity>Pa.s</viscosity>
+      <viscosityOfLiquid>Pa.s</viscosityOfLiquid>
+      <viscosityOfVapor>Pa.s</viscosityOfVapor>
+      <volume>m3</volume>
+      <volumetricFlow>m3/h</volumetricFlow>
+      <diffusivity>m2/s</diffusivity>
+      <conductance>[kg/s]/[Pa^0.5]</conductance>
+    </SelectedUnitSystem1>
+    <SimultaneousAdjustSolverEnabled>true</SimultaneousAdjustSolverEnabled>
+    <SpreadsheetUseRegionalSeparator>false</SpreadsheetUseRegionalSeparator>
+    <EnergyBalanceCheck>ShowWarning</EnergyBalanceCheck>
+    <MassBalanceCheck>ShowWarning</MassBalanceCheck>
+    <EnergyBalanceRelativeTolerance>0.01</EnergyBalanceRelativeTolerance>
+    <MassBalanceRelativeTolerance>0.01</MassBalanceRelativeTolerance>
+    <DisplayCornerPropertyList>false</DisplayCornerPropertyList>
+    <DisplayCornerPropertyListPosition>RightBottom</DisplayCornerPropertyListPosition>
+    <DisplayFloatingPropertyTables>true</DisplayFloatingPropertyTables>
+    <DisplayCornerPropertyListFontColor>DimGray</DisplayCornerPropertyListFontColor>
+    <DisplayCornerPropertyListFontName>Consolas</DisplayCornerPropertyListFontName>
+    <DisplayCornerPropertyListFontSize>8</DisplayCornerPropertyListFontSize>
+    <DisplayCornerPropertyListPadding>4</DisplayCornerPropertyListPadding>
+    <DefaultFloatingTableCompoundAmountBasis>Molar_Fractions</DefaultFloatingTableCompoundAmountBasis>
+    <DisplayFloatingTableCompoundAmounts>true</DisplayFloatingTableCompoundAmounts>
+    <SpreadsheetUnitLockingMode>true</SpreadsheetUnitLockingMode>
+    <CompoundOrderingMode>AsAdded</CompoundOrderingMode>
+    <FlowsheetControlPanelMode>false</FlowsheetControlPanelMode>
+    <SkipEquilibriumCalculationOnDefinedStreams>true</SkipEquilibriumCalculationOnDefinedStreams>
+    <ForceStreamPhase>None</ForceStreamPhase>
+    <DisplayUserDefinedPropertiesEditor>false</DisplayUserDefinedPropertiesEditor>
+    <LabelFontSize>10</LabelFontSize>
+    <FlowsheetColorTheme>2</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>false</EnabledUndoRedo>
+    <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" />
+      </ObjectType>
+      <ObjectType Value="Cooler">
+        <PropertyID Value="Flow Conductance" />
+        <PropertyID Value="Volume" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Content" />
+        <PropertyID Value="PROP_CL_0" />
+        <PropertyID Value="PROP_CL_1" />
+        <PropertyID Value="PROP_CL_2" />
+        <PropertyID Value="PROP_CL_3" />
+        <PropertyID Value="PROP_CL_4" />
+        <PropertyID Value="PROP_CL_5" />
+      </ObjectType>
+      <ObjectType Value="CustomUO" />
+      <ObjectType Value="DigitalGauge">
+        <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" />
+      </ObjectType>
+      <ObjectType Value="Filter">
+        <PropertyID Value="PROP_FT_0" />
+        <PropertyID Value="PROP_FT_1" />
+        <PropertyID Value="PROP_FT_2" />
+        <PropertyID Value="PROP_FT_3" />
+        <PropertyID Value="PROP_FT_4" />
+        <PropertyID Value="PROP_FT_5" />
+        <PropertyID Value="PROP_FT_6" />
+        <PropertyID Value="PROP_FT_7" />
+      </ObjectType>
+      <ObjectType Value="Flowsheet" />
+      <ObjectType Value="Heater">
+        <PropertyID Value="Flow Conductance" />
+        <PropertyID Value="Volume" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Content" />
+        <PropertyID Value="PROP_HT_0" />
+        <PropertyID Value="PROP_HT_1" />
+        <PropertyID Value="PROP_HT_2" />
+        <PropertyID Value="PROP_HT_3" />
+        <PropertyID Value="PROP_HT_4" />
+        <PropertyID Value="PROP_HT_5" />
+      </ObjectType>
+      <ObjectType Value="HeatExchanger">
+        <PropertyID Value="PROP_HX_0" />
+        <PropertyID Value="PROP_HX_1" />
+        <PropertyID Value="PROP_HX_2" />
+        <PropertyID Value="PROP_HX_3" />
+        <PropertyID Value="PROP_HX_4" />
+        <PropertyID Value="PROP_HX_25" />
+        <PropertyID Value="PROP_HX_26" />
+        <PropertyID Value="PROP_HX_27" />
+        <PropertyID Value="PROP_HX_28" />
+        <PropertyID Value="PROP_HX_32" />
+        <PropertyID Value="PROP_HX_33" />
+      </ObjectType>
+      <ObjectType Value="Input" />
+      <ObjectType Value="LevelGauge">
+        <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="Operating Pressure (Dynamics)" />
+        <PropertyID Value="Liquid Level" />
+        <PropertyID Value="Volume" />
+        <PropertyID Value="Height" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Contents" />
+        <PropertyID Value="PROP_CR_0" />
+        <PropertyID Value="Calculation Mode" />
+      </ObjectType>
+      <ObjectType Value="Reactor_CSTR">
+        <PropertyID Value="Operating Pressure" />
+        <PropertyID Value="Liquid Level" />
+        <PropertyID Value="Height" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Contents" />
+        <PropertyID Value="PROP_CS_0" />
+        <PropertyID Value="PROP_CS_1" />
+        <PropertyID Value="PROP_CS_2" />
+        <PropertyID Value="PROP_CS_3" />
+        <PropertyID Value="PROP_CS_4" />
+        <PropertyID Value="PROP_CS_5" />
+        <PropertyID Value="PROP_CS_6" />
+        <PropertyID Value="PROP_CS_7" />
+        <PropertyID Value="Calculation Mode" />
+      </ObjectType>
+      <ObjectType Value="Reactor_Equilibrium">
+        <PropertyID Value="Operating Pressure (Dynamics)" />
+        <PropertyID Value="Liquid Level" />
+        <PropertyID Value="Volume" />
+        <PropertyID Value="Height" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Contents" />
+        <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="Operating Pressure (Dynamics)" />
+        <PropertyID Value="Liquid Level" />
+        <PropertyID Value="Volume" />
+        <PropertyID Value="Height" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Contents" />
+        <PropertyID Value="PROP_GR_0" />
+        <PropertyID Value="PROP_GR_1" />
+        <PropertyID Value="Calculation Mode" />
+        <PropertyID Value="Initial Gibbs Energy" />
+        <PropertyID Value="Final Gibbs Energy" />
+        <PropertyID Value="Element Balance Residue" />
+      </ObjectType>
+      <ObjectType Value="Reactor_PFR">
+        <PropertyID Value="Max Sections" />
+        <PropertyID Value="Reset Contents" />
+        <PropertyID Value="PROP_PF_0" />
+        <PropertyID Value="PROP_PF_1" />
+        <PropertyID Value="PROP_PF_2" />
+        <PropertyID Value="PROP_PF_3" />
+        <PropertyID Value="PROP_PF_4" />
+        <PropertyID Value="PROP_PF_5" />
+        <PropertyID Value="PROP_PF_6" />
+        <PropertyID Value="PROP_PF_7" />
+        <PropertyID Value="PROP_PF_8" />
+        <PropertyID Value="PROP_PF_9" />
+        <PropertyID Value="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" />
+        <PropertyID Value="PROP_SC_7" />
+        <PropertyID Value="PROP_SC_8" />
+        <PropertyID Value="PROP_SC_9" />
+        <PropertyID Value="PROP_SC_10" />
+        <PropertyID Value="PROP_SC_11" />
+        <PropertyID Value="PROP_SC_12" />
+        <PropertyID Value="PROP_SC_13" />
+        <PropertyID Value="PROP_SC_14" />
+      </ObjectType>
+      <ObjectType Value="SolidsSeparator">
+        <PropertyID Value="PROP_SS_1" />
+        <PropertyID Value="PROP_SS_2" />
+      </ObjectType>
+      <ObjectType Value="Spec">
+        <PropertyID Value="SpecMin" />
+        <PropertyID Value="SpecMax" />
+        <PropertyID Value="Expression" />
+      </ObjectType>
+      <ObjectType Value="Splitter">
+        <PropertyID Value="PROP_SP_1" />
+        <PropertyID Value="PROP_SP_2" />
+      </ObjectType>
+      <ObjectType Value="Switch" />
+      <ObjectType Value="Tank">
+        <PropertyID Value="Liquid Level" />
+        <PropertyID Value="Height" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Content" />
+        <PropertyID Value="PROP_TK_0" />
+        <PropertyID Value="PROP_TK_1" />
+        <PropertyID Value="PROP_TK_2" />
+      </ObjectType>
+      <ObjectType Value="Valve">
+        <PropertyID Value="Actuator Delay" />
+        <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="Vessel Orientation" />
+        <PropertyID Value="Operating Pressure" />
+        <PropertyID Value="Liquid Level" />
+        <PropertyID Value="Volume" />
+        <PropertyID Value="Height" />
+        <PropertyID Value="Minimum Pressure" />
+        <PropertyID Value="Initialize using Inlet Stream" />
+        <PropertyID Value="Reset Content" />
+        <PropertyID Value="PROP_SV_0" />
+        <PropertyID Value="PROP_SV_1" />
+      </ObjectType>
+      <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="AirCooler2">
+        <PropertyID Value="Outlet Temperature" />
+        <PropertyID Value="Overall UA" />
+        <PropertyID Value="Heat Load" />
+        <PropertyID Value="Electrical Power Load" />
+        <PropertyID Value="Actual Air Flow" />
+        <PropertyID Value="Air Inlet Temperature" />
+        <PropertyID Value="Air Outlet Temperature" />
+        <PropertyID Value="Max Heat Exchange" />
+        <PropertyID Value="Exchanger Efficiency" />
+      </ObjectType>
+      <ObjectType Value="EnergyMixer" />
+      <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>
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+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
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+      <GradientMode>true</GradientMode>
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+      <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-5da372cf-beda-4763-98f1-cd86c5e18f47</Name>
+      <Tag>Make-up</Tag>
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+      <Rotation>0</Rotation>
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+      <GradientMode>true</GradientMode>
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+      <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-db971471-1e8a-42d3-ad06-be461cacea57</Name>
+      <Tag>Solvent Recovery</Tag>
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+      <GradientMode>true</GradientMode>
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+      <FontStyle>Bold</FontStyle>
+      <Calculated>true</Calculated>
+      <Active>true</Active>
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+      <Status>Calculated</Status>
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+      <FontStyle>Bold</FontStyle>
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+      <Status>Calculated</Status>
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+      <IsConnector>false</IsConnector>
+      <Name>MIST-ae80e666-b984-4270-b427-05f406124fe0</Name>
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+      <FontStyle>Bold</FontStyle>
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+      <Active>true</Active>
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+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CAPEOPENGraphic</Type>
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+      <FontStyle>Bold</FontStyle>
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+      <Active>true</Active>
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+      <FlippedV>false</FlippedV>
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+      <ObjectType>CapeOpenUO</ObjectType>
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+      <ShapeOverride>DefaultShape</ShapeOverride>
+      <Status>Calculated</Status>
+      <AutoSize>false</AutoSize>
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+      <Name>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</Name>
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+      <DrawMode>2</DrawMode>
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+      <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-03b2c90d-8474-4909-bef0-39eb7b0a6f41</Name>
+      <Tag>S-02</Tag>
+      <Width>20</Width>
+      <X>653.9861</X>
+      <Y>42.16959</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="COUO-1ea327c9-e43b-4061-8522-62cdfff084b8" 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>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name>
+      <Tag>Water</Tag>
+      <Width>20</Width>
+      <X>638.2234</X>
+      <Y>224.5327</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694" AttachedFromConnIndex="1" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="false" />
+      </OutputConnectors>
+      <EnergyConnector>
+        <Connector IsAttached="false" />
+      </EnergyConnector>
+      <SpecialConnectors />
+    </GraphicObject>
+    <GraphicObject>
+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CAPEOPENGraphic</Type>
+      <ChemSep>true</ChemSep>
+      <SemiTransparent>false</SemiTransparent>
+      <LineWidth>1</LineWidth>
+      <GradientMode>true</GradientMode>
+      <LineColor>#ff4682b4</LineColor>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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>CAPE-OPEN Unit Operation Block</Description>
+      <FlippedH>false</FlippedH>
+      <FlippedV>false</FlippedV>
+      <IsEnergyStream>false</IsEnergyStream>
+      <ObjectType>CapeOpenUO</ObjectType>
+      <Shape>0</Shape>
+      <ShapeOverride>DefaultShape</ShapeOverride>
+      <Status>Calculated</Status>
+      <AutoSize>false</AutoSize>
+      <Height>180</Height>
+      <IsConnector>false</IsConnector>
+      <Name>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</Name>
+      <Tag>DC-01</Tag>
+      <Width>144</Width>
+      <X>720.1278</X>
+      <Y>42.01218</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-03b2c90d-8474-4909-bef0-39eb7b0a6f41" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-8945f5e3-1173-41b4-b25e-51fbfe116943" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225" 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>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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-8945f5e3-1173-41b4-b25e-51fbfe116943</Name>
+      <Tag>Acetone</Tag>
+      <Width>20</Width>
+      <X>925.4</X>
+      <Y>48.04378</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="COUO-1ea327c9-e43b-4061-8522-62cdfff084b8" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="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>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name>
+      <Tag>3-Methylhexane</Tag>
+      <Width>20</Width>
+      <X>891.114</X>
+      <Y>228.9925</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="COUO-1ea327c9-e43b-4061-8522-62cdfff084b8" AttachedFromConnIndex="1" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="RESF-26c14620-b257-493a-b6d0-b997b40f8564" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+      </OutputConnectors>
+      <EnergyConnector>
+        <Connector IsAttached="false" />
+      </EnergyConnector>
+      <SpecialConnectors />
+    </GraphicObject>
+    <GraphicObject>
+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CoolerGraphic</Type>
+      <SemiTransparent>false</SemiTransparent>
+      <LineWidth>1</LineWidth>
+      <GradientMode>true</GradientMode>
+      <LineColor>#ff4682b4</LineColor>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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 Cooler</Description>
+      <FlippedH>false</FlippedH>
+      <FlippedV>false</FlippedV>
+      <IsEnergyStream>false</IsEnergyStream>
+      <ObjectType>Cooler</ObjectType>
+      <Shape>0</Shape>
+      <ShapeOverride>DefaultShape</ShapeOverride>
+      <Status>Calculated</Status>
+      <AutoSize>false</AutoSize>
+      <Height>25</Height>
+      <IsConnector>false</IsConnector>
+      <Name>RESF-26c14620-b257-493a-b6d0-b997b40f8564</Name>
+      <Tag>CL-01</Tag>
+      <Width>25</Width>
+      <X>742.8982</X>
+      <Y>278.1421</Y>
+      <Selected>false</Selected>
+      <Rotation>180</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+        <Connector IsAttached="false" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-7163e870-a957-43da-8cc9-c5c97bbddd42" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+      </OutputConnectors>
+      <EnergyConnector AttachedFromObjID="RESF-26c14620-b257-493a-b6d0-b997b40f8564" AttachedFromConnIndex="-1" AttachedFromEnergyConn="False">
+        <Connector IsAttached="true" AttachedToObjID="EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd" AttachedToConnIndex="0" AttachedToEnergyConn="True" />
+      </EnergyConnector>
+      <SpecialConnectors />
+    </GraphicObject>
+    <GraphicObject>
+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+      <SemiTransparent>false</SemiTransparent>
+      <LineWidth>1</LineWidth>
+      <GradientMode>true</GradientMode>
+      <LineColor>#ff4682b4</LineColor>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <FillColor>#ffd3d3d3</FillColor>
+      <FillColorDark>#ffffffff</FillColorDark>
+      <GradientColor1>#ffd3d3d3</GradientColor1>
+      <GradientColor2>#ffffffff</GradientColor2>
+      <FontSize>10</FontSize>
+      <OverrideColors>false</OverrideColors>
+      <FontStyle>Bold</FontStyle>
+      <Calculated>true</Calculated>
+      <Active>true</Active>
+      <Description>Energy Stream</Description>
+      <FlippedH>false</FlippedH>
+      <FlippedV>false</FlippedV>
+      <IsEnergyStream>true</IsEnergyStream>
+      <ObjectType>EnergyStream</ObjectType>
+      <Shape>0</Shape>
+      <ShapeOverride>DefaultShape</ShapeOverride>
+      <Status>Calculated</Status>
+      <AutoSize>false</AutoSize>
+      <Height>20</Height>
+      <IsConnector>false</IsConnector>
+      <Name>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name>
+      <Tag>E-01</Tag>
+      <Width>20</Width>
+      <X>764.0726</X>
+      <Y>315.2731</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="RESF-26c14620-b257-493a-b6d0-b997b40f8564" AttachedFromConnIndex="-1" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="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>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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-7163e870-a957-43da-8cc9-c5c97bbddd42</Name>
+      <Tag>S-03</Tag>
+      <Width>20</Width>
+      <X>640.9811</X>
+      <Y>288.7796</Y>
+      <Selected>false</Selected>
+      <Rotation>181</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="RESF-26c14620-b257-493a-b6d0-b997b40f8564" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+      </OutputConnectors>
+      <EnergyConnector>
+        <Connector IsAttached="false" />
+      </EnergyConnector>
+      <SpecialConnectors />
+    </GraphicObject>
+    <GraphicObject>
+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.RecycleGraphic</Type>
+      <SemiTransparent>false</SemiTransparent>
+      <LineWidth>1</LineWidth>
+      <GradientMode>true</GradientMode>
+      <LineColor>#ff4682b4</LineColor>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>true</Fill>
+      <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>Recycle Logical Op</Description>
+      <FlippedH>false</FlippedH>
+      <FlippedV>false</FlippedV>
+      <IsEnergyStream>false</IsEnergyStream>
+      <ObjectType>OT_Recycle</ObjectType>
+      <Shape>0</Shape>
+      <ShapeOverride>DefaultShape</ShapeOverride>
+      <Status>Calculated</Status>
+      <AutoSize>false</AutoSize>
+      <Height>20</Height>
+      <IsConnector>false</IsConnector>
+      <Name>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</Name>
+      <Tag>R-1</Tag>
+      <Width>20</Width>
+      <X>411.9529</X>
+      <Y>261.9022</Y>
+      <Selected>false</Selected>
+      <Rotation>180</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors>
+        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-7163e870-a957-43da-8cc9-c5c97bbddd42" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+      </InputConnectors>
+      <OutputConnectors>
+        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-db971471-1e8a-42d3-ad06-be461cacea57" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+      </OutputConnectors>
+      <EnergyConnector>
+        <Connector IsAttached="false" />
+      </EnergyConnector>
+      <SpecialConnectors />
+    </GraphicObject>
+    <GraphicObject>
+      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.MasterTableGraphic</Type>
+      <ClipboardData>Master Property Table
+Object	Water	Solvent Recovery	Make-up	Feed	Acetone	3-Methylhexane
+Temperature	12.3335	25	25	25	57.7331	95.7602	C
+Pressure	1.01325	1.01325	1.01325	1.01325	1.01325	1.01325	bar
+Mass Flow	20.0582	173.272	150	100	215.979	173.272	kg/h
+Molar Flow	1.06482	2.80861	1.49698	2.62831	2.80861	2.80861	kmol/h
+Volumetric Flow	0.0201646	0.215989	0.219095	0.113715	0.304737	0.231667	m3/h
+Molar Enthalpy (Mixture)	-973.015	7.79216	14.8297	413.471	7172.99	11464.7	kJ/kmol
+Molar Entropy (Mixture)	-3.4083	0.026135	0.0497392	1.38679	21.6783	31.0771	kJ/[kmol.K]
+</ClipboardData>
+      <NumberOfLines>1</NumberOfLines>
+      <Padding>4</Padding>
+      <TextColor>#ff000000</TextColor>
+      <TextColorDark>#fff5f5f5</TextColorDark>
+      <BorderColor>#ff000000</BorderColor>
+      <BorderColorDark>#fff5f5f5</BorderColorDark>
+      <SortBy>Name | DESC</SortBy>
+      <SortedList>
+        <Item>Water</Item>
+        <Item>Solvent Recovery</Item>
+        <Item>Make-up</Item>
+        <Item>Feed</Item>
+        <Item>Acetone</Item>
+        <Item>3-Methylhexane</Item>
+      </SortedList>
+      <ObjectFamily>MaterialStream</ObjectFamily>
+      <HeaderText>Master Property Table</HeaderText>
+      <SemiTransparent>false</SemiTransparent>
+      <LineWidth>1</LineWidth>
+      <GradientMode>true</GradientMode>
+      <LineColor>#fffa8072</LineColor>
+      <LineColorDark>#fff5f5f5</LineColorDark>
+      <Fill>false</Fill>
+      <FillColor>#ffd3d3d3</FillColor>
+      <FillColorDark>#ffffffff</FillColorDark>
+      <GradientColor1>#ffd3d3d3</GradientColor1>
+      <GradientColor2>#ffffffff</GradientColor2>
+      <FontSize>10</FontSize>
+      <OverrideColors>false</OverrideColors>
+      <FontStyle>Bold</FontStyle>
+      <Calculated>false</Calculated>
+      <Active>true</Active>
+      <Description></Description>
+      <FlippedH>false</FlippedH>
+      <FlippedV>false</FlippedV>
+      <IsEnergyStream>false</IsEnergyStream>
+      <ObjectType>GO_MasterTable</ObjectType>
+      <Shape>0</Shape>
+      <ShapeOverride>DefaultShape</ShapeOverride>
+      <Status>NotCalculated</Status>
+      <AutoSize>true</AutoSize>
+      <Height>162</Height>
+      <IsConnector>false</IsConnector>
+      <Name>MASTERTABLE-94b87b53-789f-4e15-9f26-07a3eff3148b</Name>
+      <Tag></Tag>
+      <Width>719</Width>
+      <X>250.6318</X>
+      <Y>378.0211</Y>
+      <Selected>false</Selected>
+      <Rotation>0</Rotation>
+      <DrawMode>2</DrawMode>
+      <InputConnectors />
+      <OutputConnectors />
+      <EnergyConnector>
+        <Connector IsAttached="false" />
+      </EnergyConnector>
+      <SpecialConnectors />
+      <Objects>
+        <S-03>false</S-03>
+        <_x0033_-Methylhexane>true</_x0033_-Methylhexane>
+        <Acetone>true</Acetone>
+        <S-01>false</S-01>
+        <S-02>false</S-02>
+        <Water>true</Water>
+        <Feed>true</Feed>
+        <Solvent_x0020_Recovery>true</Solvent_x0020_Recovery>
+        <Make-up>true</Make-up>
+      </Objects>
+      <Properties>
+        <PROP_MS_0>true</PROP_MS_0>
+        <PROP_MS_1>true</PROP_MS_1>
+        <PROP_MS_2>true</PROP_MS_2>
+        <PROP_MS_3>true</PROP_MS_3>
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+        <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Acetone>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Acetone>
+        <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Acetone>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Acetone>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Acetone>false</Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Acetone>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Acetone>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Acetone>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Acetone>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Acetone>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Acetone>false</Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Acetone>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Acetone>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Acetone>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Acetone>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Acetone>
+        <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Water>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Water>
+        <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Water>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Water>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Water>false</Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Water>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Water>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Water>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Water>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Water>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Water>false</Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_Water>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Water>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_Water>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Water>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_Water>
+        <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_3-methylhexane>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_3-methylhexane>
+        <Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_3-methylhexane>false</Activity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_3-methylhexane>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_3-methylhexane>false</Fugacity_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_3-methylhexane>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_3-methylhexane>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_3-methylhexane>
+        <Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_3-methylhexane>false</Fugacity_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_3-methylhexane>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_3-methylhexane>false</Diffusion_x0020_Coefficient_x002C__x0020_Vapor_x0020_Phase_x0020__x002F__x0020_3-methylhexane>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_3-methylhexane>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_1_x0020__x002F__x0020_3-methylhexane>
+        <Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_3-methylhexane>false</Diffusion_x0020_Coefficient_x002C__x0020_Liquid_x0020_Phase_x0020_2_x0020__x002F__x0020_3-methylhexane>
+        <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>
+      </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>Volumetric Flow | ASC</SortableItem>
+        <SortableItem>Volumetric Flow | DESC</SortableItem>
+        <SortableItem>Molar Enthalpy (Mixture) | ASC</SortableItem>
+        <SortableItem>Molar Enthalpy (Mixture) | DESC</SortableItem>
+        <SortableItem>Molar Entropy (Mixture) | ASC</SortableItem>
+        <SortableItem>Molar Entropy (Mixture) | DESC</SortableItem>
+        <SortableItem>Custom</SortableItem>
+      </SortableItems>
+    </GraphicObject>
+  </GraphicObjects>
+  <PropertyPackages>
+    <PropertyPackage>
+      <ID>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</ID>
+      <Type>DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage</Type>
+      <ComponentName>NRTL</ComponentName>
+      <ComponentDescription>Uses NRTL (Non-Random Two-Liquid) model to calculate liquid-phase activity coefficients.</ComponentDescription>
+      <Tag>NRTL (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>LiqCp_Excess</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>
+      <ForcedSolids>[]</ForcedSolids>
+      <PropertyOverrides>{}</PropertyOverrides>
+      <InteractionParameters_PR />
+      <InteractionParameters_NRTL>
+        <InteractionParameter Compound1="Acetone" Compound2="3-methylhexane" ID1="" ID2="" A12="292.355969237514" A21="901.544671308057" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
+        <InteractionParameter Compound1="Water" Compound2="Acetone" ID1="1921" ID2="1051" A12="1324.9767" A21="814.1435" B12="0" B21="0" C12="0" C21="0" alpha12="0.5663" />
+        <InteractionParameter Compound1="Water" Compound2="3-methylhexane" ID1="" ID2="" A12="1E-10" A21="1E-10" B12="0" B21="0" C12="0" C21="0" alpha12="1E-10" />
+      </InteractionParameters_NRTL>
+      <FlashSettings>
+        <Setting Name="Replace_PTFlash" Value="False" />
+        <Setting Name="ValidateEquilibriumCalc" Value="False" />
+        <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
+        <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
+        <Setting Name="ValidationGibbsTolerance" Value="0.01" />
+        <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+        <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+        <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
+        <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
+        <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
+        <Setting Name="NL_FastMode" Value="True" />
+        <Setting Name="IO_FastMode" Value="True" />
+        <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
+        <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
+        <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
+        <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
+        <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
+        <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
+        <Setting Name="ST_Number_of_Random_Tries" Value="20" />
+        <Setting Name="CheckIncipientLiquidForStability" Value="False" />
+        <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
+        <Setting Name="PTFlash_DampingFactor" Value="1.0" />
+        <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
+        <Setting Name="ImmiscibleWaterOption" Value="False" />
+        <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
+        <Setting Name="UseIOFlash" Value="False" />
+        <Setting Name="GibbsMinimizationExternalSolver" Value="" />
+        <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
+        <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>0.307</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>67-64-1</CAS_Number>
+      <Chao_Seader_Acentricity>0.3099</Chao_Seader_Acentricity>
+      <Chao_Seader_Liquid_Molar_Volume>73.8386</Chao_Seader_Liquid_Molar_Volume>
+      <Chao_Seader_Solubility_Parameter>0.0047123599262</Chao_Seader_Solubility_Parameter>
+      <Charge>0</Charge>
+      <ChemicalStructure></ChemicalStructure>
+      <Comments></Comments>
+      <CompCreatorStudyFile></CompCreatorStudyFile>
+      <Critical_Compressibility>0.233</Critical_Compressibility>
+      <Critical_Pressure>4700000</Critical_Pressure>
+      <Critical_Temperature>508.1</Critical_Temperature>
+      <Critical_Volume>0.209</Critical_Volume>
+      <CurrentDB>ChemSep</CurrentDB>
+      <Dipole_Moment>9.61E-30</Dipole_Moment>
+      <Electrolyte_Cp0>0</Electrolyte_Cp0>
+      <Electrolyte_DelGF>0</Electrolyte_DelGF>
+      <Electrolyte_DelHF>0</Electrolyte_DelHF>
+      <EnthalpyOfFusionAtTf>5.774</EnthalpyOfFusionAtTf>
+      <Formula>CH3COCH3</Formula>
+      <HVap_A>66943000</HVap_A>
+      <HVap_B>3.4736</HVap_B>
+      <HVap_C>-8.9271</HVap_C>
+      <HVap_D>10.062</HVap_D>
+      <HVap_E>-4.1656</HVap_E>
+      <HVap_TMAX>508.15</HVap_TMAX>
+      <HVap_TMIN>178.45</HVap_TMIN>
+      <HydrationNumber>0</HydrationNumber>
+      <ID>1051</ID>
+      <Ideal_Gas_Heat_Capacity_Const_A>52915</Ideal_Gas_Heat_Capacity_Const_A>
+      <Ideal_Gas_Heat_Capacity_Const_B>-669.27</Ideal_Gas_Heat_Capacity_Const_B>
+      <Ideal_Gas_Heat_Capacity_Const_C>12.201</Ideal_Gas_Heat_Capacity_Const_C>
+      <Ideal_Gas_Heat_Capacity_Const_D>0.00012839</Ideal_Gas_Heat_Capacity_Const_D>
+      <Ideal_Gas_Heat_Capacity_Const_E>-5.8844E-08</Ideal_Gas_Heat_Capacity_Const_E>
+      <IdealgasCpEquation>16</IdealgasCpEquation>
+      <IG_Enthalpy_of_Formation_25C>-3713.89796749745</IG_Enthalpy_of_Formation_25C>
+      <IG_Entropy_of_Formation_25C>-3.71904023360928</IG_Entropy_of_Formation_25C>
+      <IG_Gibbs_Energy_of_Formation_25C>-2605.06612184685</IG_Gibbs_Energy_of_Formation_25C>
+      <InChI></InChI>
+      <Ion_CpAq_a>0</Ion_CpAq_a>
+      <Ion_CpAq_b>0</Ion_CpAq_b>
+      <Ion_CpAq_c>0</Ion_CpAq_c>
+      <IsBlackOil>false</IsBlackOil>
+      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
+      <IsFPROPSSupported>false</IsFPROPSSupported>
+      <IsHydratedSalt>false</IsHydratedSalt>
+      <IsHYPO>0</IsHYPO>
+      <IsIon>false</IsIon>
+      <IsModified>false</IsModified>
+      <IsPF>0</IsPF>
+      <IsSalt>false</IsSalt>
+      <Liquid_Density_Const_A>1.1051</Liquid_Density_Const_A>
+      <Liquid_Density_Const_B>0.24556</Liquid_Density_Const_B>
+      <Liquid_Density_Const_C>508.21</Liquid_Density_Const_C>
+      <Liquid_Density_Const_D>0.27409</Liquid_Density_Const_D>
+      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+      <Liquid_Density_Tmax>508.2</Liquid_Density_Tmax>
+      <Liquid_Density_Tmin>178</Liquid_Density_Tmin>
+      <Liquid_Heat_Capacity_Const_A>107130</Liquid_Heat_Capacity_Const_A>
+      <Liquid_Heat_Capacity_Const_B>725.57</Liquid_Heat_Capacity_Const_B>
+      <Liquid_Heat_Capacity_Const_C>0.95296</Liquid_Heat_Capacity_Const_C>
+      <Liquid_Heat_Capacity_Const_D>0.025981</Liquid_Heat_Capacity_Const_D>
+      <Liquid_Heat_Capacity_Const_E>-1.439E-05</Liquid_Heat_Capacity_Const_E>
+      <Liquid_Heat_Capacity_Tmax>329.44</Liquid_Heat_Capacity_Tmax>
+      <Liquid_Heat_Capacity_Tmin>178.45</Liquid_Heat_Capacity_Tmin>
+      <Liquid_Thermal_Conductivity_Const_A>0.01013</Liquid_Thermal_Conductivity_Const_A>
+      <Liquid_Thermal_Conductivity_Const_B>-95.32</Liquid_Thermal_Conductivity_Const_B>
+      <Liquid_Thermal_Conductivity_Const_C>-0.21151</Liquid_Thermal_Conductivity_Const_C>
+      <Liquid_Thermal_Conductivity_Const_D>-0.0052616</Liquid_Thermal_Conductivity_Const_D>
+      <Liquid_Thermal_Conductivity_Const_E>2.3043E-06</Liquid_Thermal_Conductivity_Const_E>
+      <Liquid_Thermal_Conductivity_Tmax>343.15</Liquid_Thermal_Conductivity_Tmax>
+      <Liquid_Thermal_Conductivity_Tmin>178.45</Liquid_Thermal_Conductivity_Tmin>
+      <Liquid_Viscosity_Const_A>-14.064</Liquid_Viscosity_Const_A>
+      <Liquid_Viscosity_Const_B>1000.7</Liquid_Viscosity_Const_B>
+      <Liquid_Viscosity_Const_C>0.45349</Liquid_Viscosity_Const_C>
+      <Liquid_Viscosity_Const_D>3.9456E-07</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>58.07914</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>Acetone</Name>
+      <NBP>329.22</NBP>
+      <NegativeIon></NegativeIon>
+      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+      <Normal_Boiling_Point>329.22</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(=O)C</SMILES>
+      <Solid_Density_Const_A>16.677</Solid_Density_Const_A>
+      <Solid_Density_Const_B>1.103E-09</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>183.65</Solid_Density_Tmax>
+      <Solid_Density_Tmin>174.15</Solid_Density_Tmin>
+      <Solid_Heat_Capacity_Const_A>-13993</Solid_Heat_Capacity_Const_A>
+      <Solid_Heat_Capacity_Const_B>1377</Solid_Heat_Capacity_Const_B>
+      <Solid_Heat_Capacity_Const_C>-8.1059</Solid_Heat_Capacity_Const_C>
+      <Solid_Heat_Capacity_Const_D>0.029271</Solid_Heat_Capacity_Const_D>
+      <Solid_Heat_Capacity_Const_E>-4.792E-05</Solid_Heat_Capacity_Const_E>
+      <Solid_Heat_Capacity_Tmax>178.45</Solid_Heat_Capacity_Tmax>
+      <Solid_Heat_Capacity_Tmin>25</Solid_Heat_Capacity_Tmin>
+      <SolidDensityAtTs>0</SolidDensityAtTs>
+      <SolidDensityEquation>2</SolidDensityEquation>
+      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
+      <SolidTs>0</SolidTs>
+      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
+      <StandardStateMolarVolume>0</StandardStateMolarVolume>
+      <StoichSum>0</StoichSum>
+      <Surface_Tension_Const_A>-0.036769</Surface_Tension_Const_A>
+      <Surface_Tension_Const_B>-1.4835</Surface_Tension_Const_B>
+      <Surface_Tension_Const_C>-2.315</Surface_Tension_Const_C>
+      <Surface_Tension_Const_D>-0.0012473</Surface_Tension_Const_D>
+      <Surface_Tension_Const_E>-1.404E-06</Surface_Tension_Const_E>
+      <Surface_Tension_Tmax>490.84</Surface_Tension_Tmax>
+      <Surface_Tension_Tmin>178.45</Surface_Tension_Tmin>
+      <SurfaceTensionEquation>16</SurfaceTensionEquation>
+      <TemperatureOfFusion>178.45</TemperatureOfFusion>
+      <UNIQUAC_Q>2.336</UNIQUAC_Q>
+      <UNIQUAC_R>2.5735</UNIQUAC_R>
+      <Vapor_Pressure_Constant_A>72.77713</Vapor_Pressure_Constant_A>
+      <Vapor_Pressure_Constant_B>-5752.936</Vapor_Pressure_Constant_B>
+      <Vapor_Pressure_Constant_C>-7.680083</Vapor_Pressure_Constant_C>
+      <Vapor_Pressure_Constant_D>6.83076E-06</Vapor_Pressure_Constant_D>
+      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+      <Vapor_Pressure_TMAX>508.2</Vapor_Pressure_TMAX>
+      <Vapor_Pressure_TMIN>178.45</Vapor_Pressure_TMIN>
+      <Vapor_Thermal_Conductivity_Const_A>-26.882</Vapor_Thermal_Conductivity_Const_A>
+      <Vapor_Thermal_Conductivity_Const_B>0.9036</Vapor_Thermal_Conductivity_Const_B>
+      <Vapor_Thermal_Conductivity_Const_C>-120950000</Vapor_Thermal_Conductivity_Const_C>
+      <Vapor_Thermal_Conductivity_Const_D>-608790000</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>178.45</Vapor_Thermal_Conductivity_Tmin>
+      <Vapor_Viscosity_Const_A>3.1012E-08</Vapor_Viscosity_Const_A>
+      <Vapor_Viscosity_Const_B>0.97616</Vapor_Viscosity_Const_B>
+      <Vapor_Viscosity_Const_C>23.042</Vapor_Viscosity_Const_C>
+      <Vapor_Viscosity_Const_D>14.834</Vapor_Viscosity_Const_D>
+      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
+      <Vapor_Viscosity_Tmin>178.45</Vapor_Viscosity_Tmin>
+      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+      <VaporPressureEquation>101</VaporPressureEquation>
+      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+      <VaporViscosityEquation>102</VaporViscosityEquation>
+      <Z_Rackett>0</Z_Rackett>
+      <FullerDiffusionVolume>67.67</FullerDiffusionVolume>
+      <LennardJonesDiameter>4.5E-10</LennardJonesDiameter>
+      <LennardJonesEnergy>549</LennardJonesEnergy>
+      <Parachor>0.0289</Parachor>
+      <Tag></Tag>
+      <COSTALD_SRK_Acentric_Factor>0.3149</COSTALD_SRK_Acentric_Factor>
+      <COSTALD_Characteristic_Volume>0.20983</COSTALD_Characteristic_Volume>
+      <IsSolid>false</IsSolid>
+      <ChemSepFamily>26</ChemSepFamily>
+      <DynamicProperties />
+      <UNIFACGroups>
+        <Item GroupID="1" Value="1" />
+        <Item GroupID="19" Value="1" />
+      </UNIFACGroups>
+      <MODFACGroups>
+        <Item GroupID="1" Value="1" />
+        <Item GroupID="18" Value="1" />
+      </MODFACGroups>
+      <NISTMODFACGroups>
+        <Item GroupID="1" Value="1" />
+        <Item GroupID="18" Value="1" />
+      </NISTMODFACGroups>
+      <Elements>
+        <Item Name="C" Value="3" />
+        <Item Name="H" Value="6" />
+        <Item Name="O" Value="1" />
+      </Elements>
+    </Compound>
+    <Compound>
+      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+      <Acentric_Factor>0.344</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>7732-18-5</CAS_Number>
+      <Chao_Seader_Acentricity>0.328</Chao_Seader_Acentricity>
+      <Chao_Seader_Liquid_Molar_Volume>18.0674</Chao_Seader_Liquid_Molar_Volume>
+      <Chao_Seader_Solubility_Parameter>0.0114198721442</Chao_Seader_Solubility_Parameter>
+      <Charge>0</Charge>
+      <ChemicalStructure></ChemicalStructure>
+      <Comments></Comments>
+      <CompCreatorStudyFile></CompCreatorStudyFile>
+      <Critical_Compressibility>0.229</Critical_Compressibility>
+      <Critical_Pressure>22064000</Critical_Pressure>
+      <Critical_Temperature>647.14</Critical_Temperature>
+      <Critical_Volume>0.05595</Critical_Volume>
+      <CurrentDB>ChemSep</CurrentDB>
+      <Dipole_Moment>6.17E-30</Dipole_Moment>
+      <Electrolyte_Cp0>0</Electrolyte_Cp0>
+      <Electrolyte_DelGF>0</Electrolyte_DelGF>
+      <Electrolyte_DelHF>0</Electrolyte_DelHF>
+      <EnthalpyOfFusionAtTf>6.00174</EnthalpyOfFusionAtTf>
+      <Formula>HOH</Formula>
+      <HVap_A>59640000</HVap_A>
+      <HVap_B>0.86515</HVap_B>
+      <HVap_C>-1.1134</HVap_C>
+      <HVap_D>0.67764</HVap_D>
+      <HVap_E>-0.026925</HVap_E>
+      <HVap_TMAX>647.28</HVap_TMAX>
+      <HVap_TMIN>273.15</HVap_TMIN>
+      <HydrationNumber>0</HydrationNumber>
+      <ID>1921</ID>
+      <Ideal_Gas_Heat_Capacity_Const_A>33200</Ideal_Gas_Heat_Capacity_Const_A>
+      <Ideal_Gas_Heat_Capacity_Const_B>-878.9001</Ideal_Gas_Heat_Capacity_Const_B>
+      <Ideal_Gas_Heat_Capacity_Const_C>8.436956</Ideal_Gas_Heat_Capacity_Const_C>
+      <Ideal_Gas_Heat_Capacity_Const_D>0.00207627</Ideal_Gas_Heat_Capacity_Const_D>
+      <Ideal_Gas_Heat_Capacity_Const_E>-6.467085E-07</Ideal_Gas_Heat_Capacity_Const_E>
+      <IdealgasCpEquation>16</IdealgasCpEquation>
+      <IG_Enthalpy_of_Formation_25C>-13422.7167160322</IG_Enthalpy_of_Formation_25C>
+      <IG_Entropy_of_Formation_25C>-2.4619941145636</IG_Entropy_of_Formation_25C>
+      <IG_Gibbs_Energy_of_Formation_25C>-12688.673170775</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>32.51621</Liquid_Density_Const_A>
+      <Liquid_Density_Const_B>-3.213004</Liquid_Density_Const_B>
+      <Liquid_Density_Const_C>7.92411</Liquid_Density_Const_C>
+      <Liquid_Density_Const_D>-7.359898</Liquid_Density_Const_D>
+      <Liquid_Density_Const_E>2.703522</Liquid_Density_Const_E>
+      <Liquid_Density_Tmax>647.29</Liquid_Density_Tmax>
+      <Liquid_Density_Tmin>253.1</Liquid_Density_Tmin>
+      <Liquid_Heat_Capacity_Const_A>75539</Liquid_Heat_Capacity_Const_A>
+      <Liquid_Heat_Capacity_Const_B>-22297</Liquid_Heat_Capacity_Const_B>
+      <Liquid_Heat_Capacity_Const_C>136.02</Liquid_Heat_Capacity_Const_C>
+      <Liquid_Heat_Capacity_Const_D>-0.25622</Liquid_Heat_Capacity_Const_D>
+      <Liquid_Heat_Capacity_Const_E>0.00018273</Liquid_Heat_Capacity_Const_E>
+      <Liquid_Heat_Capacity_Tmax>533.15</Liquid_Heat_Capacity_Tmax>
+      <Liquid_Heat_Capacity_Tmin>273.1</Liquid_Heat_Capacity_Tmin>
+      <Liquid_Thermal_Conductivity_Const_A>-1.5697</Liquid_Thermal_Conductivity_Const_A>
+      <Liquid_Thermal_Conductivity_Const_B>-55.141</Liquid_Thermal_Conductivity_Const_B>
+      <Liquid_Thermal_Conductivity_Const_C>0.7832</Liquid_Thermal_Conductivity_Const_C>
+      <Liquid_Thermal_Conductivity_Const_D>0.0011484</Liquid_Thermal_Conductivity_Const_D>
+      <Liquid_Thermal_Conductivity_Const_E>-1.8151E-06</Liquid_Thermal_Conductivity_Const_E>
+      <Liquid_Thermal_Conductivity_Tmax>633.15</Liquid_Thermal_Conductivity_Tmax>
+      <Liquid_Thermal_Conductivity_Tmin>273.1</Liquid_Thermal_Conductivity_Tmin>
+      <Liquid_Viscosity_Const_A>-133.7</Liquid_Viscosity_Const_A>
+      <Liquid_Viscosity_Const_B>6785.7</Liquid_Viscosity_Const_B>
+      <Liquid_Viscosity_Const_C>18.47</Liquid_Viscosity_Const_C>
+      <Liquid_Viscosity_Const_D>-1.4736E-05</Liquid_Viscosity_Const_D>
+      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+      <LiquidDensityEquation>106</LiquidDensityEquation>
+      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
+      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
+      <LiquidViscosityEquation>101</LiquidViscosityEquation>
+      <Molar_Weight>18.01528</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>Water</Name>
+      <NBP>373.15</NBP>
+      <NegativeIon></NegativeIon>
+      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+      <Normal_Boiling_Point>373.15</Normal_Boiling_Point>
+      <OriginalDB>ChemSep</OriginalDB>
+      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
+      <PC_SAFT_m>0</PC_SAFT_m>
+      <PC_SAFT_sigma>0</PC_SAFT_sigma>
+      <PositiveIon></PositiveIon>
+      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
+      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
+      <SMILES>O</SMILES>
+      <Solid_Density_Const_A>52.967</Solid_Density_Const_A>
+      <Solid_Density_Const_B>-0.0075822</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>273.15</Solid_Density_Tmax>
+      <Solid_Density_Tmin>233.15</Solid_Density_Tmin>
+      <Solid_Heat_Capacity_Const_A>-262.51</Solid_Heat_Capacity_Const_A>
+      <Solid_Heat_Capacity_Const_B>140.52</Solid_Heat_Capacity_Const_B>
+      <Solid_Heat_Capacity_Const_C>-3.8869E-06</Solid_Heat_Capacity_Const_C>
+      <Solid_Heat_Capacity_Const_D>-1.1996E-08</Solid_Heat_Capacity_Const_D>
+      <Solid_Heat_Capacity_Const_E>7.1879E-11</Solid_Heat_Capacity_Const_E>
+      <Solid_Heat_Capacity_Tmax>273.15</Solid_Heat_Capacity_Tmax>
+      <Solid_Heat_Capacity_Tmin>3.15</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>
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+      <Surface_Tension_Const_C>-3.6781</Surface_Tension_Const_C>
+      <Surface_Tension_Const_D>0.0053717</Surface_Tension_Const_D>
+      <Surface_Tension_Const_E>-8.4188E-06</Surface_Tension_Const_E>
+      <Surface_Tension_Tmax>647.1</Surface_Tension_Tmax>
+      <Surface_Tension_Tmin>265.1</Surface_Tension_Tmin>
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+      <UNIQUAC_Q>1.4</UNIQUAC_Q>
+      <UNIQUAC_R>0.92</UNIQUAC_R>
+      <Vapor_Pressure_Constant_A>74.55502</Vapor_Pressure_Constant_A>
+      <Vapor_Pressure_Constant_B>-7295.586</Vapor_Pressure_Constant_B>
+      <Vapor_Pressure_Constant_C>-7.442448</Vapor_Pressure_Constant_C>
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+      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+      <Vapor_Pressure_TMAX>647.29</Vapor_Pressure_TMAX>
+      <Vapor_Pressure_TMIN>263.15</Vapor_Pressure_TMIN>
+      <Vapor_Thermal_Conductivity_Const_A>6.5986E-06</Vapor_Thermal_Conductivity_Const_A>
+      <Vapor_Thermal_Conductivity_Const_B>1.3947</Vapor_Thermal_Conductivity_Const_B>
+      <Vapor_Thermal_Conductivity_Const_C>59.478</Vapor_Thermal_Conductivity_Const_C>
+      <Vapor_Thermal_Conductivity_Const_D>-15484</Vapor_Thermal_Conductivity_Const_D>
+      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
+      <Vapor_Thermal_Conductivity_Tmax>1073.15</Vapor_Thermal_Conductivity_Tmax>
+      <Vapor_Thermal_Conductivity_Tmin>273.16</Vapor_Thermal_Conductivity_Tmin>
+      <Vapor_Viscosity_Const_A>7.002327E-08</Vapor_Viscosity_Const_A>
+      <Vapor_Viscosity_Const_B>0.934576</Vapor_Viscosity_Const_B>
+      <Vapor_Viscosity_Const_C>195.6338</Vapor_Viscosity_Const_C>
+      <Vapor_Viscosity_Const_D>-13045.99</Vapor_Viscosity_Const_D>
+      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+      <Vapor_Viscosity_Tmax>1073.15</Vapor_Viscosity_Tmax>
+      <Vapor_Viscosity_Tmin>273.16</Vapor_Viscosity_Tmin>
+      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+      <VaporPressureEquation>101</VaporPressureEquation>
+      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+      <VaporViscosityEquation>102</VaporViscosityEquation>
+      <Z_Rackett>0.2338</Z_Rackett>
+      <FullerDiffusionVolume>13.11</FullerDiffusionVolume>
+      <LennardJonesDiameter>2.52E-10</LennardJonesDiameter>
+      <LennardJonesEnergy>775</LennardJonesEnergy>
+      <Parachor>0.00926</Parachor>
+      <Tag></Tag>
+      <COSTALD_SRK_Acentric_Factor>-0.65445</COSTALD_SRK_Acentric_Factor>
+      <COSTALD_Characteristic_Volume>0.04357</COSTALD_Characteristic_Volume>
+      <IsSolid>false</IsSolid>
+      <ChemSepFamily>84</ChemSepFamily>
+      <DynamicProperties />
+      <UNIFACGroups>
+        <Item GroupID="17" Value="1" />
+      </UNIFACGroups>
+      <MODFACGroups>
+        <Item GroupID="16" Value="1" />
+      </MODFACGroups>
+      <NISTMODFACGroups>
+        <Item GroupID="16" Value="1" />
+      </NISTMODFACGroups>
+      <Elements>
+        <Item Name="H" Value="2" />
+        <Item Name="O" Value="1" />
+      </Elements>
+    </Compound>
+    <Compound>
+      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+      <Acentric_Factor>0.323</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>589-34-4</CAS_Number>
+      <Chao_Seader_Acentricity>0.323</Chao_Seader_Acentricity>
+      <Chao_Seader_Liquid_Molar_Volume>146.74</Chao_Seader_Liquid_Molar_Volume>
+      <Chao_Seader_Solubility_Parameter>0.0035707477</Chao_Seader_Solubility_Parameter>
+      <Charge>0</Charge>
+      <ChemicalStructure></ChemicalStructure>
+      <Comments></Comments>
+      <CompCreatorStudyFile></CompCreatorStudyFile>
+      <Critical_Compressibility>0.255</Critical_Compressibility>
+      <Critical_Pressure>2810000</Critical_Pressure>
+      <Critical_Temperature>535.2</Critical_Temperature>
+      <Critical_Volume>0.404</Critical_Volume>
+      <CurrentDB>ChemSep</CurrentDB>
+      <Dipole_Moment>0</Dipole_Moment>
+      <Electrolyte_Cp0>0</Electrolyte_Cp0>
+      <Electrolyte_DelGF>0</Electrolyte_DelGF>
+      <Electrolyte_DelHF>0</Electrolyte_DelHF>
+      <EnthalpyOfFusionAtTf>9.46</EnthalpyOfFusionAtTf>
+      <Formula>CH3CH2CH(CH3)CH2CH2CH3</Formula>
+      <HVap_A>58177680</HVap_A>
+      <HVap_B>1.085699</HVap_B>
+      <HVap_C>-1.05321</HVap_C>
+      <HVap_D>0.37877</HVap_D>
+      <HVap_E>0.0254378</HVap_E>
+      <HVap_TMAX>515.12</HVap_TMAX>
+      <HVap_TMIN>153.75</HVap_TMIN>
+      <HydrationNumber>0</HydrationNumber>
+      <ID>19</ID>
+      <Ideal_Gas_Heat_Capacity_Const_A>80171</Ideal_Gas_Heat_Capacity_Const_A>
+      <Ideal_Gas_Heat_Capacity_Const_B>-511.41</Ideal_Gas_Heat_Capacity_Const_B>
+      <Ideal_Gas_Heat_Capacity_Const_C>12.979</Ideal_Gas_Heat_Capacity_Const_C>
+      <Ideal_Gas_Heat_Capacity_Const_D>0.00025345</Ideal_Gas_Heat_Capacity_Const_D>
+      <Ideal_Gas_Heat_Capacity_Const_E>-8.5984E-08</Ideal_Gas_Heat_Capacity_Const_E>
+      <IdealgasCpEquation>16</IdealgasCpEquation>
+      <IG_Enthalpy_of_Formation_25C>-1909.44292529091</IG_Enthalpy_of_Formation_25C>
+      <IG_Entropy_of_Formation_25C>-6.57434350547497</IG_Entropy_of_Formation_25C>
+      <IG_Gibbs_Energy_of_Formation_25C>50.6975908664498</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>false</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>0.53784</Liquid_Density_Const_A>
+      <Liquid_Density_Const_B>0.24926</Liquid_Density_Const_B>
+      <Liquid_Density_Const_C>535.2</Liquid_Density_Const_C>
+      <Liquid_Density_Const_D>0.22945</Liquid_Density_Const_D>
+      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+      <Liquid_Density_Tmax>535.19</Liquid_Density_Tmax>
+      <Liquid_Density_Tmin>153.75</Liquid_Density_Tmin>
+      <Liquid_Heat_Capacity_Const_A>151720</Liquid_Heat_Capacity_Const_A>
+      <Liquid_Heat_Capacity_Const_B>437.07</Liquid_Heat_Capacity_Const_B>
+      <Liquid_Heat_Capacity_Const_C>3.0907</Liquid_Heat_Capacity_Const_C>
+      <Liquid_Heat_Capacity_Const_D>0.032504</Liquid_Heat_Capacity_Const_D>
+      <Liquid_Heat_Capacity_Const_E>-3.4822E-05</Liquid_Heat_Capacity_Const_E>
+      <Liquid_Heat_Capacity_Tmax>365</Liquid_Heat_Capacity_Tmax>
+      <Liquid_Heat_Capacity_Tmin>153.75</Liquid_Heat_Capacity_Tmin>
+      <Liquid_Thermal_Conductivity_Const_A>-0.14432</Liquid_Thermal_Conductivity_Const_A>
+      <Liquid_Thermal_Conductivity_Const_B>11.474</Liquid_Thermal_Conductivity_Const_B>
+      <Liquid_Thermal_Conductivity_Const_C>-1.2132</Liquid_Thermal_Conductivity_Const_C>
+      <Liquid_Thermal_Conductivity_Const_D>-0.00022172</Liquid_Thermal_Conductivity_Const_D>
+      <Liquid_Thermal_Conductivity_Const_E>-1.0949E-06</Liquid_Thermal_Conductivity_Const_E>
+      <Liquid_Thermal_Conductivity_Tmax>425</Liquid_Thermal_Conductivity_Tmax>
+      <Liquid_Thermal_Conductivity_Tmin>153.75</Liquid_Thermal_Conductivity_Tmin>
+      <Liquid_Viscosity_Const_A>-11.794</Liquid_Viscosity_Const_A>
+      <Liquid_Viscosity_Const_B>999.53</Liquid_Viscosity_Const_B>
+      <Liquid_Viscosity_Const_C>0.086997</Liquid_Viscosity_Const_C>
+      <Liquid_Viscosity_Const_D>-2.3727E-07</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>100.202</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>3-methylhexane</Name>
+      <NBP>365</NBP>
+      <NegativeIon></NegativeIon>
+      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+      <Normal_Boiling_Point>365</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>CCC(C)CCC</SMILES>
+      <Solid_Density_Const_A>9.934</Solid_Density_Const_A>
+      <Solid_Density_Const_B>-0.007197</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>153.75</Solid_Density_Tmax>
+      <Solid_Density_Tmin>61.5</Solid_Density_Tmin>
+      <Solid_Heat_Capacity_Const_A>-60717</Solid_Heat_Capacity_Const_A>
+      <Solid_Heat_Capacity_Const_B>5410</Solid_Heat_Capacity_Const_B>
+      <Solid_Heat_Capacity_Const_C>-46.69</Solid_Heat_Capacity_Const_C>
+      <Solid_Heat_Capacity_Const_D>0.17474</Solid_Heat_Capacity_Const_D>
+      <Solid_Heat_Capacity_Const_E>-0.00023062</Solid_Heat_Capacity_Const_E>
+      <Solid_Heat_Capacity_Tmax>289.2</Solid_Heat_Capacity_Tmax>
+      <Solid_Heat_Capacity_Tmin>89.2</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>-0.014185</Surface_Tension_Const_A>
+      <Surface_Tension_Const_B>14.535</Surface_Tension_Const_B>
+      <Surface_Tension_Const_C>-2.9491</Surface_Tension_Const_C>
+      <Surface_Tension_Const_D>-0.00055881</Surface_Tension_Const_D>
+      <Surface_Tension_Const_E>-3.7071E-06</Surface_Tension_Const_E>
+      <Surface_Tension_Tmax>515.12</Surface_Tension_Tmax>
+      <Surface_Tension_Tmin>153.75</Surface_Tension_Tmin>
+      <SurfaceTensionEquation>16</SurfaceTensionEquation>
+      <TemperatureOfFusion>153.75</TemperatureOfFusion>
+      <UNIQUAC_Q>4.392</UNIQUAC_Q>
+      <UNIQUAC_R>5.1734</UNIQUAC_R>
+      <Vapor_Pressure_Constant_A>86.76736</Vapor_Pressure_Constant_A>
+      <Vapor_Pressure_Constant_B>-6773.074</Vapor_Pressure_Constant_B>
+      <Vapor_Pressure_Constant_C>-9.77749</Vapor_Pressure_Constant_C>
+      <Vapor_Pressure_Constant_D>7.535909E-06</Vapor_Pressure_Constant_D>
+      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+      <Vapor_Pressure_TMAX>535.2</Vapor_Pressure_TMAX>
+      <Vapor_Pressure_TMIN>153.75</Vapor_Pressure_TMIN>
+      <Vapor_Thermal_Conductivity_Const_A>4.1038E-05</Vapor_Thermal_Conductivity_Const_A>
+      <Vapor_Thermal_Conductivity_Const_B>1.1288</Vapor_Thermal_Conductivity_Const_B>
+      <Vapor_Thermal_Conductivity_Const_C>-121.44</Vapor_Thermal_Conductivity_Const_C>
+      <Vapor_Thermal_Conductivity_Const_D>150080</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>153.75</Vapor_Thermal_Conductivity_Tmin>
+      <Vapor_Viscosity_Const_A>4.5226E-07</Vapor_Viscosity_Const_A>
+      <Vapor_Viscosity_Const_B>0.55481</Vapor_Viscosity_Const_B>
+      <Vapor_Viscosity_Const_C>210.53</Vapor_Viscosity_Const_C>
+      <Vapor_Viscosity_Const_D>14.061</Vapor_Viscosity_Const_D>
+      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
+      <Vapor_Viscosity_Tmin>153.75</Vapor_Viscosity_Tmin>
+      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+      <VaporPressureEquation>101</VaporPressureEquation>
+      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+      <VaporViscosityEquation>102</VaporViscosityEquation>
+      <Z_Rackett>0.255</Z_Rackett>
+      <FullerDiffusionVolume>148.26</FullerDiffusionVolume>
+      <LennardJonesDiameter>7.109797E-10</LennardJonesDiameter>
+      <LennardJonesEnergy>255.2548</LennardJonesEnergy>
+      <Parachor>0.0540085</Parachor>
+      <Tag></Tag>
+      <COSTALD_SRK_Acentric_Factor>0.323</COSTALD_SRK_Acentric_Factor>
+      <COSTALD_Characteristic_Volume>0.425893</COSTALD_Characteristic_Volume>
+      <IsSolid>false</IsSolid>
+      <ChemSepFamily>2</ChemSepFamily>
+      <DynamicProperties />
+      <UNIFACGroups>
+        <Item GroupID="1" Value="3" />
+        <Item GroupID="2" Value="3" />
+        <Item GroupID="3" Value="1" />
+      </UNIFACGroups>
+      <MODFACGroups>
+        <Item GroupID="1" Value="3" />
+        <Item GroupID="2" Value="3" />
+        <Item GroupID="3" Value="1" />
+      </MODFACGroups>
+      <NISTMODFACGroups>
+        <Item GroupID="1" Value="3" />
+        <Item GroupID="2" Value="3" />
+        <Item GroupID="3" Value="1" />
+      </NISTMODFACGroups>
+      <Elements>
+        <Item Name="C" Value="7" />
+        <Item Name="H" Value="16" />
+      </Elements>
+    </Compound>
+  </Compounds>
+  <ReactionSets>
+    <ReactionSet>
+      <ID>DefaultSet</ID>
+      <Name>Default Set</Name>
+      <Description>Default Reaction Set</Description>
+      <Reactions />
+    </ReactionSet>
+  </ReactionSets>
+  <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 />
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+  </OptimizationCases>
+  <SensitivityAnalysis>
+    <SensitivityAnalysisCase>
+      <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SensitivityAnalysisCase</Type>
+      <iv1>
+        <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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+        <name></name>
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+      <dv>
+        <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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+        <propID></propID>
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+        <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>
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+        <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 />
+  <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>&lt;?xml version="1.0" encoding="utf-8"?&gt;
+&lt;!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.--&gt;
+&lt;!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!--&gt;
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+  &lt;Contents Count="10"&gt;
+    &lt;Content ID="0" PersistString="DWSIM.LogPanel" AutoHidePortion="0.152227705943669" IsHidden="True" IsFloat="False" /&gt;
+    &lt;Content ID="1" PersistString="DWSIM.MaterialStreamPanel" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
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+    &lt;Content ID="9" PersistString="DWSIM.FormScript" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
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+    &lt;/Pane&gt;
+  &lt;/Panes&gt;
+  &lt;DockWindows&gt;
+    &lt;DockWindow ID="0" DockState="Document" ZOrderIndex="1"&gt;
+      &lt;NestedPanes Count="1"&gt;
+        &lt;Pane ID="0" RefID="0" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
+      &lt;/NestedPanes&gt;
+    &lt;/DockWindow&gt;
+    &lt;DockWindow ID="1" DockState="DockLeft" ZOrderIndex="4"&gt;
+      &lt;NestedPanes Count="0" /&gt;
+    &lt;/DockWindow&gt;
+    &lt;DockWindow ID="2" DockState="DockRight" ZOrderIndex="2"&gt;
+      &lt;NestedPanes Count="0" /&gt;
+    &lt;/DockWindow&gt;
+    &lt;DockWindow ID="3" DockState="DockTop" ZOrderIndex="5"&gt;
+      &lt;NestedPanes Count="0" /&gt;
+    &lt;/DockWindow&gt;
+    &lt;DockWindow ID="4" DockState="DockBottom" ZOrderIndex="3"&gt;
+      &lt;NestedPanes Count="3"&gt;
+        &lt;Pane ID="0" RefID="1" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
+        &lt;Pane ID="1" RefID="4" PrevPane="1" Alignment="Top" Proportion="0.5" /&gt;
+        &lt;Pane ID="2" RefID="2" PrevPane="1" Alignment="Right" Proportion="0.261838440111421" /&gt;
+      &lt;/NestedPanes&gt;
+    &lt;/DockWindow&gt;
+  &lt;/DockWindows&gt;
+  &lt;FloatWindows Count="1"&gt;
+    &lt;FloatWindow ID="0" Bounds="336, 370, 900, 155" ZOrderIndex="0"&gt;
+      &lt;NestedPanes Count="1"&gt;
+        &lt;Pane ID="0" RefID="3" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
+      &lt;/NestedPanes&gt;
+    &lt;/FloatWindow&gt;
+  &lt;/FloatWindows&gt;
+&lt;/DockPanel&gt;</PanelLayout>
+  <MessagesLog>
+    <Message>[11/12/2023 1:24:58 AM] Estimated NRTL IP set for Acetone/3-methylhexane: 292.36/901.54/0.2</Message>
+    <Message>[11/12/2023 1:27:14 AM] When running simulations containing CAPE-OPEN unit ops in another computer, make sure that these components are installed and registered properly on it.</Message>
+    <Message>[11/12/2023 1:30:59 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          0           7.9743</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          1           7.3867</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          2           7.1773</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          3           7.0893</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          4           6.8834</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          5           6.7619</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          6           7.1867</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          7           6.9010</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          8           6.5132</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:          9           6.3219</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         10           6.0883</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         11           6.3229</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         12           6.5202</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         13           6.5834</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         14           6.4361</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         15           6.5522</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         16           6.7521</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         17           6.6120</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         18           6.7010</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         19           6.6811</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         20           6.6648</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         21           6.6001</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         22           6.6678</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         23           6.6997</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         24           6.9882</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         25           6.6346</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         26           6.4823</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         27           6.4919</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         28           6.4737</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         29           6.4166</Message>
+    <Message>[11/12/2023 1:31:01 AM] EDC-01:         30           6.5008</Message>
+    <Message>[11/12/2023 1:31:01 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:31:01 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:31:02 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          0           7.9743</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          1           7.3867</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          2           7.1773</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          3           7.0893</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          4           6.8834</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          5           6.7619</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          6           7.1867</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          7           6.9010</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          8           6.5132</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:          9           6.3219</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         10           6.0883</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         11           6.3229</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         12           6.5202</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         13           6.5834</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         14           6.4361</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         15           6.5522</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         16           6.7521</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         17           6.6120</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         18           6.7010</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         19           6.6811</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         20           6.6648</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         21           6.6001</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         22           6.6678</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         23           6.6997</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         24           6.9882</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         25           6.6346</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         26           6.4823</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         27           6.4919</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         28           6.4737</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         29           6.4166</Message>
+    <Message>[11/12/2023 1:31:08 AM] EDC-01:         30           6.5008</Message>
+    <Message>[11/12/2023 1:31:08 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:31:08 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:31:09 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:31:09 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:31:34 AM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          0           7.9743</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          1           7.3867</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          2           7.1773</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          3           7.0893</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          4           6.8834</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          5           6.7619</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          6           7.1867</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          7           6.9010</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          8           6.5132</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:          9           6.3219</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         10           6.0883</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         11           6.3229</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         12           6.5202</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         13           6.5834</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         14           6.4361</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         15           6.5522</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         16           6.7521</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         17           6.6120</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         18           6.7010</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         19           6.6811</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         20           6.6648</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         21           6.6001</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         22           6.6678</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         23           6.6997</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         24           6.9882</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         25           6.6346</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         26           6.4823</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         27           6.4919</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         28           6.4737</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         29           6.4166</Message>
+    <Message>[11/12/2023 1:31:50 AM] EDC-01:         30           6.5008</Message>
+    <Message>[11/12/2023 1:31:50 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:31:51 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:31:51 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:31:51 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:32:11 AM] When running simulations containing CAPE-OPEN unit ops in another computer, make sure that these components are installed and registered properly on it.</Message>
+    <Message>[11/12/2023 1:34:13 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:34:13 AM] The flowsheet was calculated successfully. [0.005122s]</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          0           7.9554</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          1           7.3996</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          2           7.2532</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          3           7.0286</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          4           6.9185</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          5           6.7421</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          6           6.6389</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          7           6.5974</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          8           6.5627</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:          9           6.9032</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         10           6.9018</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         11           6.6340</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         12           6.8620</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         13           6.8659</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         14           6.8552</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         15           6.7674</Message>
+    <Message>[11/12/2023 1:34:24 AM] EDC-01:         16           7.1182</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         17           7.0790</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         18           7.0635</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         19           7.1730</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         20           7.2390</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         21           7.1940</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         22           6.9702</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         23           7.0919</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         24           6.9060</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         25           7.1235</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         26           6.8859</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         27           7.0953</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         28           6.9047</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         29           6.5136</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01:         30           6.8553</Message>
+    <Message>[11/12/2023 1:34:25 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:34:25 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:34:25 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:34:25 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:34:25 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:34:25 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          0           7.9554</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          1           7.3996</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          2           7.2532</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          3           7.0286</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          4           6.9185</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          5           6.7421</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          6           6.6389</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          7           6.5974</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          8           6.5627</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:          9           6.9032</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         10           6.9018</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         11           6.6340</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         12           6.8620</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         13           6.8659</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         14           6.8552</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         15           6.7674</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         16           7.1182</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         17           7.0790</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         18           7.0635</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         19           7.1730</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         20           7.2390</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         21           7.1940</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         22           6.9702</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         23           7.0919</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         24           6.9060</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         25           7.1235</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         26           6.8859</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         27           7.0953</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         28           6.9047</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         29           6.5136</Message>
+    <Message>[11/12/2023 1:34:26 AM] EDC-01:         30           6.8553</Message>
+    <Message>[11/12/2023 1:34:26 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:34:26 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:34:26 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          0           7.9554</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          1           7.3996</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          2           7.2532</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          3           7.0286</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          4           6.9185</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          5           6.7421</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          6           6.6389</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          7           6.5974</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          8           6.5627</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:          9           6.9032</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:         10           6.9018</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:         11           6.6340</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:         12           6.8620</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:         13           6.8659</Message>
+    <Message>[11/12/2023 1:34:37 AM] EDC-01:         14           6.8552</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         15           6.7674</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         16           7.1182</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         17           7.0790</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         18           7.0635</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         19           7.1730</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         20           7.2390</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         21           7.1940</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         22           6.9702</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         23           7.0919</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         24           6.9060</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         25           7.1235</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         26           6.8859</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         27           7.0953</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         28           6.9047</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         29           6.5136</Message>
+    <Message>[11/12/2023 1:34:38 AM] EDC-01:         30           6.8553</Message>
+    <Message>[11/12/2023 1:34:38 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:34:38 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:34:38 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:34:38 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          0           7.9554</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          1           7.3996</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          2           7.2532</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          3           7.0286</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          4           6.9185</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          5           6.7421</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          6           6.6389</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          7           6.5974</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          8           6.5627</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:          9           6.9032</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         10           6.9018</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         11           6.6340</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         12           6.8620</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         13           6.8659</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         14           6.8552</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         15           6.7674</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         16           7.1182</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         17           7.0790</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         18           7.0635</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         19           7.1730</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         20           7.2390</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         21           7.1940</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         22           6.9702</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         23           7.0919</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         24           6.9060</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         25           7.1235</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         26           6.8859</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         27           7.0953</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         28           6.9047</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         29           6.5136</Message>
+    <Message>[11/12/2023 1:34:42 AM] EDC-01:         30           6.8553</Message>
+    <Message>[11/12/2023 1:34:42 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:34:43 AM] CSCOL-1: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:34:43 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:34:43 AM] Error in 'CSCOL-1': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:35:28 AM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+    <Message>[11/12/2023 1:35:43 AM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          0           7.9554</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          1           7.3996</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          2           7.2532</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          3           7.0286</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          4           6.9185</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          5           6.7421</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          6           6.6389</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          7           6.5974</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          8           6.5627</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:          9           6.9032</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         10           6.9018</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         11           6.6340</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         12           6.8620</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         13           6.8659</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         14           6.8552</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         15           6.7674</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         16           7.1182</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         17           7.0790</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         18           7.0635</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         19           7.1730</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         20           7.2390</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         21           7.1940</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         22           6.9702</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         23           7.0919</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         24           6.9060</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         25           7.1235</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         26           6.8859</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         27           7.0953</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         28           6.9047</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         29           6.5136</Message>
+    <Message>[11/12/2023 1:35:50 AM] EDC-01:         30           6.8553</Message>
+    <Message>[11/12/2023 1:35:50 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:35:51 AM] EDC-01: CAPE-OPEN Exception 0 at ICapeUnit:Calculate. Reason: run failed: the ChemSep run did not finish successfully (for more info, see full output in report)</Message>
+    <Message>[11/12/2023 1:35:51 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
+    <Message>[11/12/2023 1:35:51 AM] Error in 'EDC-01': Exception from HRESULT: 0x80040501 (CapeOpenUO.vb, 1077)</Message>
+    <Message>[11/12/2023 1:36:07 AM] When running simulations containing CAPE-OPEN unit ops in another computer, make sure that these components are installed and registered properly on it.</Message>
+    <Message>[11/12/2023 1:38:37 AM] When running simulations containing CAPE-OPEN unit ops in another computer, make sure that these components are installed and registered properly on it.</Message>
+    <Message>[11/12/2023 1:40:49 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:40:49 AM] The flowsheet was calculated successfully. [0.003268s]</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          0           7.8974</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          1           7.5942</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          2           7.1581</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          3           7.1085</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          4           6.9443</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          5           6.8869</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          6           6.7488</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          7           6.8274</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          8           6.8472</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:          9           6.7447</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         10           6.9300</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         11           6.9014</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         12           6.7697</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         13           6.7432</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         14           6.5667</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         15           6.7614</Message>
+    <Message>[11/12/2023 1:40:59 AM] CSCOL-1:         16           6.5898</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         17           6.4261</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         18           6.3261</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         19           6.2986</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         20           6.3365</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         21           6.1723</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         22           6.0414</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         23           5.7857</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         24           5.6296</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         25           4.9022</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         26           3.5469</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         27           0.9422</Message>
+    <Message>[11/12/2023 1:41:00 AM] CSCOL-1:         28          -3.1526</Message>
+    <Message>[11/12/2023 1:41:00 AM] Warning: product port "bottom product" is not connected and has non-zero flow rate</Message>
+    <Message>[11/12/2023 1:41:00 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:41:04 AM] The flowsheet was calculated successfully. [5.809s]</Message>
+    <Message>[11/12/2023 1:41:13 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:41:13 AM] The flowsheet was calculated successfully. [0.005597s]</Message>
+    <Message>[11/12/2023 1:43:07 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:43:07 AM] The flowsheet was calculated successfully. [0.008464s]</Message>
+    <Message>[11/12/2023 1:44:11 AM] When running simulations containing CAPE-OPEN unit ops in another computer, make sure that these components are installed and registered properly on it.</Message>
+    <Message>[11/12/2023 1:49:58 AM] CSCOL-1: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:49:58 AM] CSCOL-1:          0           2.7014</Message>
+    <Message>[11/12/2023 1:49:58 AM] CSCOL-1:          1          -0.7116</Message>
+    <Message>[11/12/2023 1:49:58 AM] Warning: CSCOL-1: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+    <Message>[11/12/2023 1:49:58 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:50:02 AM] The flowsheet was calculated successfully. [3.729s]</Message>
+    <Message>[11/12/2023 1:50:15 AM] CSCOL-1: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 1:50:15 AM] CSCOL-1:          0           2.7014</Message>
+    <Message>[11/12/2023 1:50:15 AM] CSCOL-1:          1          -0.7116</Message>
+    <Message>[11/12/2023 1:50:15 AM] Warning: CSCOL-1: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+    <Message>[11/12/2023 1:50:16 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:50:19 AM] Caught unhandled exception: The requested connection between the given objects cannot be done.</Message>
+    <Message>[11/12/2023 1:50:25 AM] CSCOL-2:          0           2.1290</Message>
+    <Message>[11/12/2023 1:50:25 AM] CSCOL-2:          1           4.0755</Message>
+    <Message>[11/12/2023 1:50:25 AM] CSCOL-2:          2           3.0379</Message>
+    <Message>[11/12/2023 1:50:26 AM] CSCOL-2:          3           0.0275</Message>
+    <Message>[11/12/2023 1:50:26 AM] CSCOL-2:          4          -3.0430</Message>
+    <Message>[11/12/2023 1:50:30 AM] The flowsheet was calculated successfully. [14.55s]</Message>
+    <Message>[11/12/2023 1:50:53 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:50:53 AM] The flowsheet was calculated successfully. [0.01858s]</Message>
+    <Message>[11/12/2023 1:58:37 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 1:58:37 AM] The flowsheet was calculated successfully. [0.03557s]</Message>
+    <Message>[11/12/2023 1:58:54 AM] It is important to properly define the location of the Recycle in the flowsheet, to avoid unnecessary calculations. Insert it into the nearest point where the calculation flow returns to an already calculated point.</Message>
+    <Message>[11/12/2023 2:00:05 AM] CSCOL-1: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 2:00:05 AM] CSCOL-1:          0           2.7014</Message>
+    <Message>[11/12/2023 2:00:05 AM] CSCOL-1:          1          -0.7116</Message>
+    <Message>[11/12/2023 2:00:05 AM] Warning: CSCOL-1: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+    <Message>[11/12/2023 2:00:05 AM] The flowsheet is being calculated, please wait...</Message>
+    <Message>[11/12/2023 2:00:05 AM] Solvent Recovery: Single-compound Stream detected. Switching to PH Flash</Message>
+    <Message>[11/12/2023 2:00:08 AM] CSCOL-2:          0           2.4473</Message>
+    <Message>[11/12/2023 2:00:08 AM] CSCOL-2:          1          -0.3679</Message>
+    <Message>[11/12/2023 2:00:13 AM] Recycle loop #1, average recycle error: 33.01%</Message>
+    <Message>[11/12/2023 2:00:13 AM] CSCOL-1: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 2:00:13 AM] CSCOL-1:          0           2.9100</Message>
+    <Message>[11/12/2023 2:00:13 AM] CSCOL-1:          1           5.2157</Message>
+    <Message>[11/12/2023 2:00:13 AM] CSCOL-1:          2           4.4895</Message>
+    <Message>[11/12/2023 2:00:13 AM] CSCOL-1:          3           2.5703</Message>
+    <Message>[11/12/2023 2:00:13 AM] CSCOL-1:          4          -1.0374</Message>
+    <Message>[11/12/2023 2:00:13 AM] Warning: CSCOL-1: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+    <Message>[11/12/2023 2:00:17 AM] CSCOL-2:          0           2.8106</Message>
+    <Message>[11/12/2023 2:00:17 AM] CSCOL-2:          1           5.8264</Message>
+    <Message>[11/12/2023 2:00:17 AM] CSCOL-2:          2           5.5490</Message>
+    <Message>[11/12/2023 2:00:17 AM] CSCOL-2:          3           4.6575</Message>
+    <Message>[11/12/2023 2:00:17 AM] CSCOL-2:          4           3.2349</Message>
+    <Message>[11/12/2023 2:00:18 AM] CSCOL-2:          5           0.6471</Message>
+    <Message>[11/12/2023 2:00:18 AM] CSCOL-2:          6          -2.8089</Message>
+    <Message>[11/12/2023 2:00:22 AM] Recycle loop #2, average recycle error: 8.66%</Message>
+    <Message>[11/12/2023 2:00:22 AM] CSCOL-1: Warning!! Estimating activity model parameters</Message>
+    <Message>[11/12/2023 2:00:22 AM] CSCOL-1:          0           2.6622</Message>
+    <Message>[11/12/2023 2:00:22 AM] CSCOL-1:          1           3.7705</Message>
+    <Message>[11/12/2023 2:00:22 AM] CSCOL-1:          2           1.8833</Message>
+    <Message>[11/12/2023 2:00:22 AM] CSCOL-1:          3          -1.9457</Message>
+    <Message>[11/12/2023 2:00:22 AM] Warning: CSCOL-1: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+    <Message>[11/12/2023 2:00:26 AM] CSCOL-2:          0           2.5559</Message>
+    <Message>[11/12/2023 2:00:26 AM] CSCOL-2:          1           4.1565</Message>
+    <Message>[11/12/2023 2:00:26 AM] CSCOL-2:          2           2.7216</Message>
+    <Message>[11/12/2023 2:00:26 AM] CSCOL-2:          3          -0.3278</Message>
+    <Message>[11/12/2023 2:00:31 AM] The flowsheet was calculated successfully. [25.89s]</Message>
+    <Message>[11/12/2023 2:03:19 AM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\ff.pdf.</Message>
+    <Message>[11/12/2023 2:06:55 AM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\gg.pdf.</Message>
+    <Message>[11/12/2023 2:11:02 AM] File //Simulate 365 Dashboard/Flowsheet1.dwxml saved successfully.</Message>
+    <Message>[11/12/2023 2:11:15 AM] File C:\Users\prati\OneDrive\Documents\Flowsheet.dwxml saved successfully.</Message>
+    <Message>[11/12/2023 2:21:31 AM] File C:\Users\prati\OneDrive\Documents\Flowsheet.dwxml saved successfully.</Message>
+    <Message>[11/13/2023 8:22:56 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\Abstract.pdf.</Message>
+    <Message>[11/13/2023 8:25:25 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\hh.svg.</Message>
+    <Message>[11/13/2023 8:33:49 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\hh.pdf.</Message>
+    <Message>[11/13/2023 8:34:21 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\ff.pdf.</Message>
+    <Message>[11/13/2023 8:36:15 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\gg.pdf.</Message>
+    <Message>[11/13/2023 8:37:14 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\gg.pdf.</Message>
+  </MessagesLog>
+</DWSIM_Simulation_Data>
+\ No newline at end of file
author	Sashi20	2023-12-16 00:20:16 +0550
committer	Sashi20	2023-12-16 00:20:16 +0550
commit	1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142 (patch)
tree	122cf478e9b208a144cd3a8e5be249ba3c59420a
parent	43bb5bc5978d5bc5ff75c156993ac7710d515502 (diff)
download	DWSIM-Flowsheets-1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142.tar.gz DWSIM-Flowsheets-1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142.tar.bz2 DWSIM-Flowsheets-1a22c7241a5cecb7bd0424ef4d9d0676bb0b4142.zip