﻿<?xml version="1.0" encoding="utf-8"?>
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      <Visible>true</Visible>
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              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
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              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
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              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
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        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</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>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
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              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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              <ComponentName>Nitrogen</ComponentName>
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              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.UnitOperations.UnitOperations.Compressor</Type>
      <ObjectClass>PressureChangers</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
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      <OutletTemperature>549.766670370581</OutletTemperature>
      <CalcMode>OutletPressure</CalcMode>
      <ProcessPath>Adiabatic</ProcessPath>
      <IgnorePhase>false</IgnorePhase>
      <PolytropicEfficiency>79.4337762425752</PolytropicEfficiency>
      <AdiabaticEfficiency>75</AdiabaticEfficiency>
      <DeltaP>1800000</DeltaP>
      <DeltaT>241.616670370581</DeltaT>
      <DeltaQ>329.941836642184</DeltaQ>
      <POut>2000000</POut>
      <AdiabaticCoefficient>1.26141941969819</AdiabaticCoefficient>
      <PolytropicCoefficient>1.33886486614831</PolytropicCoefficient>
      <AdiabaticHead>29840.4539643854</AdiabaticHead>
      <PolytropicHead>31604.5325757847</PolytropicHead>
      <EquipType></EquipType>
      <CurvesDB></CurvesDB>
      <CurveFlow>0</CurveFlow>
      <CurveEff>0</CurveEff>
      <CurveHead>0</CurveHead>
      <CurvePower>0</CurvePower>
      <Speed>1500</Speed>
      <MobileCompatible>true</MobileCompatible>
      <ComponentDescription>CompressorAdiabtico</ComponentDescription>
      <ComponentName>COMP-16912814-94f1-4d57-b70b-9175d491ce81</ComponentName>
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      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
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      <Annotation></Annotation>
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      <AttachedAdjustId></AttachedAdjustId>
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      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Source</SpecVarType>
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      <AttachedUtilities />
      <PropertyPackage>PP-f1a6f133-8bcd-4b3c-8b15-f568d76417f1</PropertyPackage>
      <Curves />
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    <SimulationObject>
      <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
      <ObjectClass>Streams</ObjectClass>
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      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
      <ComponentDescription>CorrentedeEnergia</ComponentDescription>
      <ComponentName>EN-3eb67988-9ef6-484d-baa2-aead6eb86344</ComponentName>
      <EnergyFlow>329.941836642184</EnergyFlow>
      <MobileCompatible>true</MobileCompatible>
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      <code>0</code>
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      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
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      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
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      <SpecVarType>Source</SpecVarType>
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      <DynamicPropertiesDescriptions />
      <DynamicPropertiesUnitTypes />
      <AttachedUtilities />
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    <SimulationObject>
      <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
      <ObjectClass>Streams</ObjectClass>
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      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
      <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>CorrentedeMatria</ComponentDescription>
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      <Name2>MAT-e1b53ec9-8852-426d-8dec-5022269f790a</Name2>
      <code>0</code>
      <InputComposition />
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
      <MobileCompatible>true</MobileCompatible>
      <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
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      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
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            <Compound>
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              <ComponentName>Methane</ComponentName>
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              <Molarity>262.971450180851</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>NaN</Kvalue>
              <lnKvalue>NaN</lnKvalue>
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              <MolarFlow>19.6243821182567</MolarFlow>
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              <VolumetricFraction>0.601992100169537</VolumetricFraction>
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            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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              <ComponentName>Carbon dioxide</ComponentName>
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              <Molarity>175.314300120567</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>NaN</Kvalue>
              <lnKvalue>NaN</lnKvalue>
              <MassFlow>0.575772829888946</MassFlow>
              <MolarFlow>13.0829214121711</MolarFlow>
              <Name>Carbon dioxide</Name>
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              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0.0297015478561886</VolumetricFlow>
              <VolumetricFraction>0.398007899830463</VolumetricFraction>
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            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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              <ComponentName>Nitrogen</ComponentName>
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              <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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
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          </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>
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            <enthalpy>382.116263596528</enthalpy>
            <entropy>0.2377610386215</entropy>
            <heatCapacityCp>1.78392400189792</heatCapacityCp>
            <heatCapacityCv>1.46028373256915</heatCapacityCv>
            <massflow>0.890596195045795</massflow>
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            <molar_entropy>6.47406094267148</molar_entropy>
            <molarflow>32.7073035304279</molarflow>
            <molecularWeight>27.229276</molecularWeight>
            <pressure>2000000</pressure>
            <surfaceTension>NaN</surfaceTension>
            <temperature>549.766670370581</temperature>
            <thermalConductivity>0.0596905483375299</thermalConductivity>
            <volumetric_flow>0.0746255234351889</volumetric_flow>
            <gibbs_free_energy>251.403169049734</gibbs_free_energy>
            <helmholtz_energy>-167334.139752233</helmholtz_energy>
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            <molar_gibbs_free_energy>6845.52627732988</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-4556387.47553612</molar_helmholtz_energy>
            <molar_internal_energy>-4552828.25260789</molar_internal_energy>
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            <Compound>
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              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Methane</Name>
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              <PartialVolume>3.56445077136499E-05</PartialVolume>
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              <VolumetricFraction>0</VolumetricFraction>
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            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Carbon dioxide</Name>
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              <PartialVolume>3.17966074325363E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
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              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.2558472659088E-05</PartialVolume>
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              <VolumetricFraction>0</VolumetricFraction>
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          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>OverallLiquid</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>OverallLiquid</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <massflow>0</massflow>
            <massfraction>0</massfraction>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
            <molarflow>0</molarflow>
            <molarfraction>0</molarfraction>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <volumetric_flow>0</volumetric_flow>
            <gibbs_free_energy>0</gibbs_free_energy>
            <helmholtz_energy>0</helmholtz_energy>
            <internal_energy>0</internal_energy>
            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
            <molar_internal_energy>NaN</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>3.90011362407148E-05</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0.353497316638165</MassFraction>
              <MoleFraction>0.6</MoleFraction>
              <Molarity>262.971450180851</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.999949052949697</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0.314823365156849</MassFlow>
              <MolarFlow>19.6243821182567</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>1200000</PartialPressure>
              <PartialVolume>2.28574479443682</PartialVolume>
              <VolumetricFlow>0.0449239755790004</VolumetricFlow>
              <VolumetricFraction>0.601992100169537</VolumetricFraction>
              <DiffusionCoefficient>2.20165882222252E-11</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0.0017701399465707</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0.646502683361835</MassFraction>
              <MoleFraction>0.4</MoleFraction>
              <Molarity>175.314300120567</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.991639331335966</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0.575772829888946</MassFlow>
              <MolarFlow>13.0829214121711</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>800000</PartialPressure>
              <PartialVolume>2.26683494250009</PartialVolume>
              <VolumetricFlow>0.0297015478561886</VolumetricFlow>
              <VolumetricFraction>0.398007899830463</VolumetricFraction>
              <DiffusionCoefficient>1.27063539048205E-11</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>1.15414264247565E-10</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>1.01007430504207</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DiffusionCoefficient>NaN</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Vapor</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>Vapor</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>0.99835320701873</compressibilityFactor>
            <density>11.9342036618244</density>
            <enthalpy>382.116263596528</enthalpy>
            <entropy>0.2377610386215</entropy>
            <heatCapacityCp>1.78392400189792</heatCapacityCp>
            <heatCapacityCv>1.46028373256915</heatCapacityCv>
            <jouleThomsonCoefficient>1.55487169359812E-05</jouleThomsonCoefficient>
            <kinematic_viscosity>1.81417909052744E-06</kinematic_viscosity>
            <massflow>0.890596195045795</massflow>
            <massfraction>1</massfraction>
            <molar_enthalpy>10404.7492055586</molar_enthalpy>
            <molar_entropy>6.47406094267148</molar_entropy>
            <molarflow>32.7073035304279</molarflow>
            <molarfraction>1</molarfraction>
            <molecularWeight>27.229276</molecularWeight>
            <speedOfSound>408.823848828205</speedOfSound>
            <thermalConductivity>0.0596905483375299</thermalConductivity>
            <viscosity>2.16507827453778E-05</viscosity>
            <volumetric_flow>0.0746255234351889</volumetric_flow>
            <bulk_modulus>1994646.27386401</bulk_modulus>
            <gibbs_free_energy>251.403169049734</gibbs_free_energy>
            <helmholtz_energy>-167334.139752233</helmholtz_energy>
            <internal_energy>-167203.426657686</internal_energy>
            <isothermal_compressibility>5.0134202394834E-07</isothermal_compressibility>
            <molar_gibbs_free_energy>6845.52627732988</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-4556387.47553611</molar_helmholtz_energy>
            <molar_internal_energy>-4552828.25260789</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>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>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>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>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
      <ObjectClass>Exchangers</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
      <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
      <OutletTemperature>225.15</OutletTemperature>
      <OutletVaporFraction>1</OutletVaporFraction>
      <CalcMode>OutletTemperature</CalcMode>
      <Eficiencia>100</Eficiencia>
      <DeltaT>-324.616670370581</DeltaT>
      <DeltaQ>452.218780508919</DeltaQ>
      <MobileCompatible>true</MobileCompatible>
      <ComponentDescription>Resfriador</ComponentDescription>
      <ComponentName>RESF-3e731623-a669-4c6e-865d-9485049c29c0</ComponentName>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
      <ErrorMessage></ErrorMessage>
      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Manipulated</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Source</SpecVarType>
      <Name>RESF-3e731623-a669-4c6e-865d-9485049c29c0</Name>
      <DynamicProperties>
        <Property>
          <Name>Flow Conductance</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Volume</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>101325.0</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Stream</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Reset Content</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>0.0</Data>
        </Property>
      </DynamicProperties>
      <DynamicPropertiesDescriptions>
        <Property>
          <Name>Flow Conductance</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
        </Property>
        <Property>
          <Name>Volume</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Cooler Volume"</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Stream</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
        </Property>
        <Property>
          <Name>Reset Content</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Empties the volume content on the next run."</Data>
        </Property>
      </DynamicPropertiesDescriptions>
      <DynamicPropertiesUnitTypes>
        <Property>
          <Name>Flow Conductance</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>67</Data>
        </Property>
        <Property>
          <Name>Volume</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>63</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>46</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Stream</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>66</Data>
        </Property>
        <Property>
          <Name>Reset Content</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>66</Data>
        </Property>
      </DynamicPropertiesUnitTypes>
      <AttachedUtilities />
      <PropertyPackage>PP-f1a6f133-8bcd-4b3c-8b15-f568d76417f1</PropertyPackage>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
      <ObjectClass>Streams</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
      <ComponentDescription>CorrentedeEnergia</ComponentDescription>
      <ComponentName>EN-1a15ca7f-8291-4e02-9b2c-dc0a8af6923a</ComponentName>
      <EnergyFlow>452.218780508919</EnergyFlow>
      <MobileCompatible>true</MobileCompatible>
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      <code>0</code>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
      <ErrorMessage></ErrorMessage>
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      <DynamicProperties />
      <DynamicPropertiesDescriptions />
      <DynamicPropertiesUnitTypes />
      <AttachedUtilities />
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    <SimulationObject>
      <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
      <ObjectClass>Streams</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
      <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
      <AtEquilibrium>true</AtEquilibrium>
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      <ReferenceSolvent></ReferenceSolvent>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
      <MobileCompatible>true</MobileCompatible>
      <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
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              <MolarFlow>13.0829214121711</MolarFlow>
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            </Compound>
            <Compound>
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              <MassFraction>0</MassFraction>
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              <Molarity>0</Molarity>
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              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>NaN</Kvalue>
              <lnKvalue>NaN</lnKvalue>
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              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
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              <VolumetricFraction>0</VolumetricFraction>
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          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Mixture</ComponentName>
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          <Name>Mixture</Name>
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          <Properties>
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              <DiffusionCoefficient>NaN</DiffusionCoefficient>
              <DynamicProperties />
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          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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          <ComponentName>Vapor</ComponentName>
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            <temperature>0</temperature>
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            <molar_internal_energy>-1367489.39572604</molar_internal_energy>
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        <Phase>
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              <DynamicProperties />
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              <PartialVolume>3.2558472659088E-05</PartialVolume>
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              <DiffusionCoefficient>0</DiffusionCoefficient>
              <DynamicProperties />
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          </Compounds>
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            <pressure>0</pressure>
            <speedOfSound>868.732581870163</speedOfSound>
            <temperature>0</temperature>
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            <viscosity>0.000195626131173882</viscosity>
            <volumetric_flow>0.00176070415051806</volumetric_flow>
            <bulk_modulus>381739119.505768</bulk_modulus>
            <gibbs_free_energy>-42.6029722453538</gibbs_free_energy>
            <helmholtz_energy>-2862.61726338783</helmholtz_energy>
            <internal_energy>-3391.63181724745</internal_energy>
            <isothermal_compressibility>2.61959005221861E-09</isothermal_compressibility>
            <molar_gibbs_free_energy>-1160.04808968908</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-77946.9955471518</molar_helmholtz_energy>
            <molar_internal_energy>-92351.6788422124</molar_internal_energy>
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        </Phase>
        <Phase>
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          <Compounds>
            <Compound>
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              <ComponentDescription></ComponentDescription>
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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>Methane</Name>
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              <PartialVolume>0</PartialVolume>
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            <Compound>
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              <ComponentDescription></ComponentDescription>
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              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
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              <FugacityCoeff>NaN</FugacityCoeff>
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              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
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              <PartialVolume>0</PartialVolume>
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              <VolumetricFraction>0</VolumetricFraction>
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            <Compound>
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              <ComponentDescription></ComponentDescription>
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              <Molarity>0</Molarity>
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              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
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            <pressure>0</pressure>
            <temperature>0</temperature>
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              <Molarity>0</Molarity>
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              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
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              <MolarFlow>0</MolarFlow>
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          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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          <ComponentName>Aqueous</ComponentName>
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              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>NaN</Kvalue>
              <lnKvalue>NaN</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
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              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
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          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Mixture</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>Mixture</Name>
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          <Properties>
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            <Compound>
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              <lnKvalue>0</lnKvalue>
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              <Name>Nitrogen</Name>
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          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>OverallLiquid</ComponentName>
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      <Annotation></Annotation>
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          <Name>Mixture</Name>
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          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <density>34.5244150371286</density>
            <enthalpy>-125.654579154115</enthalpy>
            <entropy>-1.13749068878106</entropy>
            <heatCapacityCp>1.51713462442942</heatCapacityCp>
            <heatCapacityCv>0.915038278517855</heatCapacityCv>
            <massflow>0.890596195045795</massflow>
            <molar_enthalpy>-3421.48321645123</molar_enthalpy>
            <molar_entropy>-30.9730479122497</molar_entropy>
            <molarflow>32.7073035304279</molarflow>
            <molecularWeight>27.229276</molecularWeight>
            <pressure>2000000</pressure>
            <surfaceTension>NaN</surfaceTension>
            <temperature>225.15</temperature>
            <thermalConductivity>0.0191815801943754</thermalConductivity>
            <volumetric_flow>0.025796127004267</volumetric_flow>
            <gibbs_free_energy>130.451449424942</gibbs_free_energy>
            <helmholtz_energy>-57799.5669983646</helmholtz_energy>
            <internal_energy>-58055.6730269436</internal_energy>
            <molar_gibbs_free_energy>3552.09852099178</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-1573840.36247896</molar_helmholtz_energy>
            <molar_internal_energy>-1580813.9442164</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>1</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.56445077136499E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.8070725863033E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.2558472659088E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>OverallLiquid</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>OverallLiquid</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <massflow>0</massflow>
            <massfraction>0</massfraction>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
            <molarflow>0</molarflow>
            <molarfraction>0</molarfraction>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <volumetric_flow>0</volumetric_flow>
            <gibbs_free_energy>0</gibbs_free_energy>
            <helmholtz_energy>0</helmholtz_energy>
            <internal_energy>0</internal_energy>
            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
            <molar_internal_energy>NaN</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0.154525015510483</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0.353497316638165</MassFraction>
              <MoleFraction>0.6</MoleFraction>
              <Molarity>760.74916653227</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.910428370590638</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0.314823365156849</MassFlow>
              <MolarFlow>19.6243821182567</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>1200000</PartialPressure>
              <PartialVolume>0.850857521761466</PartialVolume>
              <VolumetricFlow>0.0167706084666935</VolumetricFlow>
              <VolumetricFraction>0.650121177644979</VolumetricFraction>
              <DiffusionCoefficient>4.61597791260106E-12</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>2.11555304325911</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0.646502683361835</MassFraction>
              <MoleFraction>0.4</MoleFraction>
              <Molarity>507.166111021513</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.784371827184813</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0.575772829888946</MassFlow>
              <MolarFlow>13.0829214121711</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>800000</PartialPressure>
              <PartialVolume>0.686865090560964</PartialVolume>
              <VolumetricFlow>0.00902551853757349</VolumetricFlow>
              <VolumetricFraction>0.349878822355021</VolumetricFraction>
              <DiffusionCoefficient>2.66400263212154E-12</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0.0156270072387504</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>1.00320714532357</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DiffusionCoefficient>NaN</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Vapor</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>Vapor</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>0.842670497753296</compressibilityFactor>
            <density>34.5244150371286</density>
            <enthalpy>-125.654579154115</enthalpy>
            <entropy>-1.13749068878106</entropy>
            <heatCapacityCp>1.51713462442942</heatCapacityCp>
            <heatCapacityCv>0.915038278517854</heatCapacityCv>
            <jouleThomsonCoefficient>-5.26257586833266E-05</jouleThomsonCoefficient>
            <kinematic_viscosity>3.06160782574592E-07</kinematic_viscosity>
            <massflow>0.890596195045795</massflow>
            <massfraction>1</massfraction>
            <molar_enthalpy>-3421.48321645123</molar_enthalpy>
            <molar_entropy>-30.9730479122497</molar_entropy>
            <molarflow>32.7073035304279</molarflow>
            <molarfraction>1</molarfraction>
            <molecularWeight>27.229276</molecularWeight>
            <speedOfSound>218.483106701306</speedOfSound>
            <thermalConductivity>0.0191815801943754</thermalConductivity>
            <viscosity>1.05700219256973E-05</viscosity>
            <volumetric_flow>0.025796127004267</volumetric_flow>
            <bulk_modulus>1648018.39160041</bulk_modulus>
            <gibbs_free_energy>130.451449424942</gibbs_free_energy>
            <helmholtz_energy>-57799.5669983646</helmholtz_energy>
            <internal_energy>-58055.6730269436</internal_energy>
            <isothermal_compressibility>6.06789344765071E-07</isothermal_compressibility>
            <molar_gibbs_free_energy>3552.09852099178</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-1573840.36247896</molar_helmholtz_energy>
            <molar_internal_energy>-1580813.9442164</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0.0280553055931522</MassFraction>
              <MoleFraction>0.0733757543632675</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>7.88483695158986</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0.971944694406848</MassFraction>
              <MoleFraction>0.926624245636733</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.345346398812737</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>23.0288835096262</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>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>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.UnitOperations.UnitOperations.HeatExchanger</Type>
      <ObjectClass>Exchangers</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
      <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
      <IgnoreLMTDError>true</IgnoreLMTDError>
      <HeatLoss>0</HeatLoss>
      <STProperties>
        <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.HeatExchanger.STHXProperties</Type>
        <Shell_NumberOfShellsInSeries>1</Shell_NumberOfShellsInSeries>
        <Shell_NumberOfPasses>2</Shell_NumberOfPasses>
        <Shell_Di>500</Shell_Di>
        <Shell_Fouling>0</Shell_Fouling>
        <Shell_BaffleType>0</Shell_BaffleType>
        <Shell_BaffleOrientation>1</Shell_BaffleOrientation>
        <Shell_BaffleCut>20</Shell_BaffleCut>
        <Shell_BaffleSpacing>250</Shell_BaffleSpacing>
        <Shell_Fluid>1</Shell_Fluid>
        <Tube_Di>50</Tube_Di>
        <Tube_De>60</Tube_De>
        <Tube_Length>5</Tube_Length>
        <Tube_Fouling>0</Tube_Fouling>
        <Tube_PassesPerShell>2</Tube_PassesPerShell>
        <Tube_NumberPerShell>50</Tube_NumberPerShell>
        <Tube_Layout>0</Tube_Layout>
        <Tube_Pitch>70</Tube_Pitch>
        <Tube_Fluid>0</Tube_Fluid>
        <Tube_Roughness>0.045000000000000005</Tube_Roughness>
        <Shell_Roughness>0.045000000000000005</Shell_Roughness>
        <Tube_Scaling_FricCorrFactor>1.2</Tube_Scaling_FricCorrFactor>
        <Tube_ThermalConductivity>70</Tube_ThermalConductivity>
        <OverallFoulingFactor>0</OverallFoulingFactor>
        <Ft>0</Ft>
        <Fc>0</Fc>
        <Fs>0</Fs>
        <Ff>0</Ff>
        <ReT>0</ReT>
        <ReS>0</ReS>
      </STProperties>
      <LMTD_F>1</LMTD_F>
      <FlowDir>CounterCurrent</FlowDir>
      <DefinedTemperature>Cold_Fluid</DefinedTemperature>
      <ThermalEfficiency>231.422571054128</ThermalEfficiency>
      <MaxHeatExchange>171.622371092296</MaxHeatExchange>
      <MITA>0</MITA>
      <CalculationMode>CalcTempColdOut</CalculationMode>
      <OverallCoefficient>NaN</OverallCoefficient>
      <Area>1</Area>
      <DeltaP>0</DeltaP>
      <Q>397.172903685848</Q>
      <HotSidePressureDrop>0</HotSidePressureDrop>
      <ColdSidePressureDrop>0</ColdSidePressureDrop>
      <HotSideOutletTemperature>153.15</HotSideOutletTemperature>
      <ColdSideOutletTemperature>333.606189018646</ColdSideOutletTemperature>
      <LMTD>NaN</LMTD>
      <MobileCompatible>true</MobileCompatible>
      <ComponentDescription>HeatExchanger</ComponentDescription>
      <ComponentName>HE-e5c9c402-5591-4f01-9b82-02d178bab24d</ComponentName>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
      <ErrorMessage></ErrorMessage>
      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Manipulated</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Source</SpecVarType>
      <Name>HE-e5c9c402-5591-4f01-9b82-02d178bab24d</Name>
      <DynamicProperties>
        <Property>
          <Name>Cold Fluid Flow Conductance</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Hot Fluid Flow Conductance</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Volume for Cold Fluid</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Volume for Hot Fluid</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Cold Side Pressure</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>101325.0</Data>
        </Property>
        <Property>
          <Name>Hot Side Pressure</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>101325.0</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>101325.0</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Streams</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>0.0</Data>
        </Property>
        <Property>
          <Name>Reset Contents</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>0.0</Data>
        </Property>
      </DynamicProperties>
      <DynamicPropertiesDescriptions>
        <Property>
          <Name>Cold Fluid Flow Conductance</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Flow Conductance (inverse of Resistance)."</Data>
        </Property>
        <Property>
          <Name>Hot Fluid Flow Conductance</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Flow Conductance (inverse of Resistance) for the Hot Fluid."</Data>
        </Property>
        <Property>
          <Name>Volume for Cold Fluid</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Available Volume for Cold Fluid"</Data>
        </Property>
        <Property>
          <Name>Volume for Hot Fluid</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Available Volume for Cold Fluid"</Data>
        </Property>
        <Property>
          <Name>Cold Side Pressure</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Dynamic Pressure for the Cold Fluid side."</Data>
        </Property>
        <Property>
          <Name>Hot Side Pressure</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Dynamic Pressure for the Hot Fluid side."</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 Streams</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Initializes the volume contents with information from the inlet streams, if the content is null."</Data>
        </Property>
        <Property>
          <Name>Reset Contents</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Empties the volume contents on the next run."</Data>
        </Property>
      </DynamicPropertiesDescriptions>
      <DynamicPropertiesUnitTypes>
        <Property>
          <Name>Cold Fluid Flow Conductance</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>67</Data>
        </Property>
        <Property>
          <Name>Hot Fluid Flow Conductance</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>67</Data>
        </Property>
        <Property>
          <Name>Volume for Cold Fluid</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>63</Data>
        </Property>
        <Property>
          <Name>Volume for Hot Fluid</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>63</Data>
        </Property>
        <Property>
          <Name>Cold Side Pressure</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>46</Data>
        </Property>
        <Property>
          <Name>Hot Side Pressure</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>46</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>46</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Streams</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>66</Data>
        </Property>
        <Property>
          <Name>Reset Contents</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>66</Data>
        </Property>
      </DynamicPropertiesUnitTypes>
      <AttachedUtilities />
      <PropertyPackage>PP-f1a6f133-8bcd-4b3c-8b15-f568d76417f1</PropertyPackage>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
      <ObjectClass>Streams</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
      <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>CorrentedeMatria</ComponentDescription>
      <ComponentName>MAT-9edbfbc0-df95-45d2-bbe3-50d8eac70c8a</ComponentName>
      <Name2>MAT-9edbfbc0-df95-45d2-bbe3-50d8eac70c8a</Name2>
      <code>0</code>
      <InputComposition />
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
      <MobileCompatible>true</MobileCompatible>
      <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
      <ErrorMessage></ErrorMessage>
      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Manipulated</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Source</SpecVarType>
      <Name>MAT-9edbfbc0-df95-45d2-bbe3-50d8eac70c8a</Name>
      <DynamicProperties />
      <DynamicPropertiesDescriptions />
      <DynamicPropertiesUnitTypes />
      <AttachedUtilities />
      <PropertyPackage>PP-f1a6f133-8bcd-4b3c-8b15-f568d76417f1</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>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>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>NaN</Kvalue>
              <lnKvalue>NaN</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>1</MassFraction>
              <MoleFraction>1</MoleFraction>
              <Molarity>170.608159525943</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>NaN</Kvalue>
              <lnKvalue>NaN</lnKvalue>
              <MassFlow>1.99138268313156</MassFlow>
              <MolarFlow>71.0867900051961</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0.416667</VolumetricFlow>
              <VolumetricFraction>1</VolumetricFraction>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Mixture</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>Mixture</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <density>4.77931461606405</density>
            <enthalpy>-162.985215948957</enthalpy>
            <entropy>-0.972835249437075</entropy>
            <heatCapacityCp>1.05829348874113</heatCapacityCp>
            <heatCapacityCv>0.737678724640873</heatCapacityCv>
            <massflow>1.99138268313156</massflow>
            <molar_enthalpy>-4565.77004846451</molar_enthalpy>
            <molar_entropy>-27.2524229765805</molar_entropy>
            <molarflow>71.0867900051961</molarflow>
            <molecularWeight>28.0134</molecularWeight>
            <pressure>200000</pressure>
            <surfaceTension>NaN</surfaceTension>
            <temperature>143.15</temperature>
            <thermalConductivity>0.0134258742088518</thermalConductivity>
            <volumetric_flow>0.416667</volumetric_flow>
            <gibbs_free_energy>-23.7238499920397</gibbs_free_energy>
            <helmholtz_energy>-41870.7282986566</helmholtz_energy>
            <internal_energy>-42009.9896646135</internal_energy>
            <molar_gibbs_free_energy>-664.585699367004</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-1172941.46012159</molar_helmholtz_energy>
            <molar_internal_energy>-1176842.64447068</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>1</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>4.30090881488977E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.1236106825982E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.2558472659088E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>OverallLiquid</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>OverallLiquid</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <massflow>0</massflow>
            <massfraction>0</massfraction>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
            <molarflow>0</molarflow>
            <molarfraction>0</molarfraction>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <volumetric_flow>0</volumetric_flow>
            <gibbs_free_energy>0</gibbs_free_energy>
            <helmholtz_energy>0</helmholtz_energy>
            <internal_energy>0</internal_energy>
            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
            <molar_internal_energy>NaN</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0.257585925979746</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.970593164663836</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DiffusionCoefficient>NaN</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>82.2716778839848</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
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              <lnKvalue>0</lnKvalue>
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              <PartialVolume>0</PartialVolume>
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              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0.985855432494532</VolumetricFlow>
              <VolumetricFraction>1</VolumetricFraction>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Mixture</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>Mixture</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <density>2.01995405968674</density>
            <enthalpy>36.4605781845487</enthalpy>
            <entropy>-0.0860970492070902</entropy>
            <heatCapacityCp>1.04372809738242</heatCapacityCp>
            <heatCapacityCv>0.744515593519382</heatCapacityCv>
            <massflow>1.99138268313156</massflow>
            <massfraction>0</massfraction>
            <molar_enthalpy>1021.38476091504</molar_enthalpy>
            <molar_entropy>-2.4118710782579</molar_entropy>
            <molarflow>71.0867900051961</molarflow>
            <molarfraction>0</molarfraction>
            <molecularWeight>28.0134</molecularWeight>
            <pressure>200000</pressure>
            <surfaceTension>NaN</surfaceTension>
            <temperature>333.606187551564</temperature>
            <thermalConductivity>0.0279170992851242</thermalConductivity>
            <volumetric_flow>0.985855432494532</volumetric_flow>
            <gibbs_free_energy>65.1830865299654</gibbs_free_energy>
            <helmholtz_energy>-98946.9697101609</helmholtz_energy>
            <internal_energy>-98975.6922185064</internal_energy>
            <molar_gibbs_free_energy>1825.99987619853</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-2771841.04127862</molar_helmholtz_energy>
            <molar_internal_energy>-2772645.65639391</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>1</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.56445077136499E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.17966074325363E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>NaN</MassFraction>
              <MoleFraction>NaN</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>NaN</MassFlow>
              <MolarFlow>NaN</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>3.2558472659088E-05</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>OverallLiquid</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>OverallLiquid</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <massflow>0</massflow>
            <massfraction>0</massfraction>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
            <molarflow>0</molarflow>
            <molarfraction>0</molarfraction>
            <molecularWeight>NaN</molecularWeight>
            <pressure>0</pressure>
            <temperature>0</temperature>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <volumetric_flow>0</volumetric_flow>
            <gibbs_free_energy>0</gibbs_free_energy>
            <helmholtz_energy>0</helmholtz_energy>
            <internal_energy>0</internal_energy>
            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
            <molar_internal_energy>NaN</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0.00143710769526413</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.997805597201076</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DiffusionCoefficient>NaN</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0.0144872850706425</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.994913573516894</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DiffusionCoefficient>NaN</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>1.68379145191023E-05</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>1</MassFraction>
              <MoleFraction>1</MoleFraction>
              <Molarity>72.1067082070275</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0.999684757104114</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>1.99138268313156</MassFlow>
              <MolarFlow>71.0867900051961</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>200000</PartialPressure>
              <PartialVolume>13.8637057256627</PartialVolume>
              <VolumetricFlow>0.985855432494532</VolumetricFlow>
              <VolumetricFraction>1</VolumetricFraction>
              <DiffusionCoefficient>8.52797159479067E-11</DiffusionCoefficient>
              <DynamicProperties />
            </Compound>
          </Compounds>
          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
          <ComponentDescription></ComponentDescription>
          <ComponentName>Vapor</ComponentName>
          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
          <Name>Vapor</Name>
          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
          <Properties>
            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
            <compressibilityFactor>1.00002350656468</compressibilityFactor>
            <density>2.01995405968674</density>
            <enthalpy>36.4605781845487</enthalpy>
            <entropy>-0.0860970492070902</entropy>
            <heatCapacityCp>1.04372809738242</heatCapacityCp>
            <heatCapacityCv>0.744515593519382</heatCapacityCv>
            <jouleThomsonCoefficient>1.34035391593889E-05</jouleThomsonCoefficient>
            <kinematic_viscosity>9.69704354957328E-06</kinematic_viscosity>
            <massflow>1.99138268313156</massflow>
            <massfraction>1</massfraction>
            <molar_enthalpy>1021.38476091504</molar_enthalpy>
            <molar_entropy>-2.4118710782579</molar_entropy>
            <molarflow>71.0867900051961</molarflow>
            <molarfraction>1</molarfraction>
            <molecularWeight>28.0134</molecularWeight>
            <pressure>0</pressure>
            <speedOfSound>314.614711993163</speedOfSound>
            <temperature>0</temperature>
            <thermalConductivity>0.0279170992851242</thermalConductivity>
            <viscosity>1.95875824849197E-05</viscosity>
            <volumetric_flow>0.985855432494532</volumetric_flow>
            <bulk_modulus>199939.935061888</bulk_modulus>
            <gibbs_free_energy>65.1830865299654</gibbs_free_energy>
            <helmholtz_energy>-98946.9697101609</helmholtz_energy>
            <internal_energy>-98975.6922185064</internal_energy>
            <isothermal_compressibility>5.00150207456287E-06</isothermal_compressibility>
            <molar_gibbs_free_energy>1825.99987619853</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-2771841.04127862</molar_helmholtz_energy>
            <molar_internal_energy>-2772645.65639391</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>1</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>1</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>200000</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>1</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>1</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>200000</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>1</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>Nitrogen</Name>
              <PartialPressure>200000</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
            <pressure>0</pressure>
            <temperature>0</temperature>
          </Properties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
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              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
            <pressure>0</pressure>
            <temperature>0</temperature>
          </Properties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
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              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
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              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
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              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
            <pressure>0</pressure>
            <temperature>0</temperature>
          </Properties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
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              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
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              <Name>Carbon dioxide</Name>
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              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
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              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
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            <molar_enthalpy>-18525.491256398</molar_enthalpy>
            <molar_entropy>-96.5334601162752</molar_entropy>
            <molarflow>13.109139691554</molarflow>
            <molarfraction>1</molarfraction>
            <molecularWeight>43.95356592</molecularWeight>
            <speedOfSound>610.930078725046</speedOfSound>
            <thermalConductivity>0.177966324879008</thermalConductivity>
            <viscosity>0.00025195722216233</viscosity>
            <volumetric_flow>0.000485603936997021</volumetric_flow>
            <bulk_modulus>442862719.685191</bulk_modulus>
            <gibbs_free_energy>54.1214229605652</gibbs_free_energy>
            <helmholtz_energy>-2197.51203157238</helmholtz_energy>
            <internal_energy>-2673.11214161186</internal_energy>
            <isothermal_compressibility>2.25803608104753E-09</isothermal_compressibility>
            <molar_gibbs_free_energy>2378.8295317814</molar_gibbs_free_energy>
            <molar_helmholtz_energy>-96588.4899397097</molar_helmholtz_energy>
            <molar_internal_energy>-117492.810727889</molar_internal_energy>
          </Properties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>0</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </Properties>
        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Methane</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>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>Methane</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Carbon dioxide</ComponentName>
              <ActivityCoeff>0</ActivityCoeff>
              <PetroleumFraction>false</PetroleumFraction>
              <MassFraction>0</MassFraction>
              <MoleFraction>0</MoleFraction>
              <Molarity>0</Molarity>
              <Molality>0</Molality>
              <FugacityCoeff>NaN</FugacityCoeff>
              <Kvalue>0</Kvalue>
              <lnKvalue>0</lnKvalue>
              <MassFlow>0</MassFlow>
              <MolarFlow>0</MolarFlow>
              <Name>Carbon dioxide</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <DynamicProperties />
            </Compound>
            <Compound>
              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
              <ComponentDescription></ComponentDescription>
              <ComponentName>Nitrogen</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>Nitrogen</Name>
              <PartialPressure>0</PartialPressure>
              <PartialVolume>0</PartialVolume>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <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>
          </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-dc80f8cd-cbbe-4946-8f3a-65325d31e6f1</ComponentName>
      <EnergyFlow>53.1142559021018</EnergyFlow>
      <MobileCompatible>true</MobileCompatible>
      <Name2>EN-dc80f8cd-cbbe-4946-8f3a-65325d31e6f1</Name2>
      <code>0</code>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
      <ErrorMessage></ErrorMessage>
      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Manipulated</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Source</SpecVarType>
      <Name>EN-dc80f8cd-cbbe-4946-8f3a-65325d31e6f1</Name>
      <DynamicProperties />
      <DynamicPropertiesDescriptions />
      <DynamicPropertiesUnitTypes />
      <AttachedUtilities />
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
      <ObjectClass>Exchangers</ObjectClass>
      <SupportsDynamicMode>true</SupportsDynamicMode>
      <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
      <OutletTemperature>216.55</OutletTemperature>
      <OutletVaporFraction>0</OutletVaporFraction>
      <CalcMode>OutletTemperature</CalcMode>
      <Eficiencia>100</Eficiencia>
      <DeltaT>-45.7993563591975</DeltaT>
      <DeltaQ>53.1142559021018</DeltaQ>
      <MobileCompatible>true</MobileCompatible>
      <ComponentDescription>Resfriador</ComponentDescription>
      <ComponentName>RESF-9e727395-713d-4ecd-96b0-4f46a98e237f</ComponentName>
      <DynamicsSpec>Pressure</DynamicsSpec>
      <DynamicsOnly>false</DynamicsOnly>
      <Visible>true</Visible>
      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
      <Calculated>true</Calculated>
      <DebugMode>false</DebugMode>
      <ErrorMessage></ErrorMessage>
      <Annotation></Annotation>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Manipulated</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Source</SpecVarType>
      <Name>RESF-9e727395-713d-4ecd-96b0-4f46a98e237f</Name>
      <DynamicProperties>
        <Property>
          <Name>Flow Conductance</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Volume</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>101325.0</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Stream</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>1.0</Data>
        </Property>
        <Property>
          <Name>Reset Content</Name>
          <PropertyType>System.Double</PropertyType>
          <Data>0.0</Data>
        </Property>
      </DynamicProperties>
      <DynamicPropertiesDescriptions>
        <Property>
          <Name>Flow Conductance</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
        </Property>
        <Property>
          <Name>Volume</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Cooler Volume"</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Stream</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
        </Property>
        <Property>
          <Name>Reset Content</Name>
          <PropertyType>System.String</PropertyType>
          <Data>"Empties the volume content on the next run."</Data>
        </Property>
      </DynamicPropertiesDescriptions>
      <DynamicPropertiesUnitTypes>
        <Property>
          <Name>Flow Conductance</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>67</Data>
        </Property>
        <Property>
          <Name>Volume</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>63</Data>
        </Property>
        <Property>
          <Name>Minimum Pressure</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>46</Data>
        </Property>
        <Property>
          <Name>Initialize using Inlet Stream</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>66</Data>
        </Property>
        <Property>
          <Name>Reset Content</Name>
          <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
          <Data>66</Data>
        </Property>
      </DynamicPropertiesUnitTypes>
      <AttachedUtilities />
      <PropertyPackage>PP-f1a6f133-8bcd-4b3c-8b15-f568d76417f1</PropertyPackage>
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  <Settings>
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    <SelectedPropertyPackage>
      <Type>DWSIM.Thermodynamics.PropertyPackages.PengRobinsonPropertyPackage</Type>
      <ComponentName>Peng-Robinson (PR)</ComponentName>
      <ComponentDescription>Property Package that uses the Peng-Robinson Cubic Equation of State. Recommended for use with hydrocarbons and non-condensables.</ComponentDescription>
      <Tag>Peng-Robinson (PR) (1)</Tag>
      <TPSeverity>0</TPSeverity>
      <TPCompIDs></TPCompIDs>
      <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
      <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
      <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
      <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
      <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
      <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
      <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
      <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
      <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
      <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
      <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
      <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
      <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
      <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
      <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
      <EnthalpyEntropyCpCvCalculationMode>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
      <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
      <ActivityCoefficientModels_IgnoreMissingInteractionParameters>true</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
      <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
      <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
      <ForcedSolids>[]</ForcedSolids>
      <PropertyOverrides>{}</PropertyOverrides>
      <InteractionParameters />
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    <SimulationMode></SimulationMode>
    <BackupFileName>89750788.dwbcs</BackupFileName>
    <FilePath></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>0750C2E89FB1B601D640C059352B88888E2F2896</Key>
    <NumberFormat>G6</NumberFormat>
    <Password></Password>
    <SimulationAuthor>AKSHAY\mehta</SimulationAuthor>
    <SimulationComments></SimulationComments>
    <SimulationName>MySimulation_18</SimulationName>
    <UsePassword>false</UsePassword>
    <SelectedUnitSystem1>
      <Type>DWSIM.SharedClasses.SystemsOfUnits.SIUnits_Custom5</Type>
      <accel>m/s2</accel>
      <activity>Pa</activity>
      <activityCoefficient>-</activityCoefficient>
      <area>m2</area>
      <cakeresistance>m/kg</cakeresistance>
      <cinematic_viscosity>m2/s</cinematic_viscosity>
      <compressibility>1/Pa</compressibility>
      <compressibilityFactor>-</compressibilityFactor>
      <deltaP>bar</deltaP>
      <deltaT>C.</deltaT>
      <density>kg/m3</density>
      <diameter>mm</diameter>
      <distance>m</distance>
      <enthalpy>kJ/kg</enthalpy>
      <entropy>kJ/[kg.K]</entropy>
      <excessEnthalpy>kJ/kg</excessEnthalpy>
      <excessEntropy>kJ/[kg.K]</excessEntropy>
      <force>N</force>
      <foulingfactor>K.m2/W</foulingfactor>
      <fugacity>Pa</fugacity>
      <fugacityCoefficient>-</fugacityCoefficient>
      <head>m</head>
      <heat_transf_coeff>W/[m2.K]</heat_transf_coeff>
      <heatCapacityCp>kJ/[kg.K]</heatCapacityCp>
      <heatCapacityCv>kJ/[kg.K]</heatCapacityCv>
      <heatflow>kW</heatflow>
      <idealGasHeatCapacity>kJ/[kg.K]</idealGasHeatCapacity>
      <jouleThomsonCoefficient>K/Pa</jouleThomsonCoefficient>
      <kvalue>-</kvalue>
      <logFugacityCoefficient>-</logFugacityCoefficient>
      <logKvalue>-</logKvalue>
      <mass>kg</mass>
      <mass_conc>kg/m3</mass_conc>
      <massflow>kg/h</massflow>
      <massfraction>-</massfraction>
      <mediumresistance>m-1</mediumresistance>
      <molar_conc>kmol/m3</molar_conc>
      <molar_enthalpy>kJ/kmol</molar_enthalpy>
      <molar_entropy>kJ/[kmol.K]</molar_entropy>
      <molar_volume>m3/kmol</molar_volume>
      <molarflow>kmol/h</molarflow>
      <molarfraction>-</molarfraction>
      <molecularWeight>kg/kmol</molecularWeight>
      <Name>C5</Name>
      <pdp_boilingPointTemperature>C</pdp_boilingPointTemperature>
      <pdp_meltingTemperature>C</pdp_meltingTemperature>
      <pressure>kPa</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>
    <VisibleProperties>
      <ObjectType Value="AbsorptionColumn">
        <PropertyID Value="PROP_AC_0" />
        <PropertyID Value="PROP_AC_1" />
        <PropertyID Value="PROP_AC_2" />
      </ObjectType>
      <ObjectType Value="Adjust">
        <PropertyID Value="MinVal" />
        <PropertyID Value="MaxVal" />
        <PropertyID Value="AdjustValue" />
        <PropertyID Value="Tolerance" />
        <PropertyID Value="StepSize" />
        <PropertyID Value="MaximumIterations" />
      </ObjectType>
      <ObjectType Value="AnalogGauge" />
      <ObjectType Value="CapeOpenUO" />
      <ObjectType Value="ComponentSeparator">
        <PropertyID Value="PROP_CP_0" />
        <PropertyID Value="SpecifiedStreamIndex" />
      </ObjectType>
      <ObjectType Value="Compressor">
        <PropertyID Value="PROP_CO_0" />
        <PropertyID Value="PROP_CO_1" />
        <PropertyID Value="PROP_CO_2" />
        <PropertyID Value="PROP_CO_3" />
        <PropertyID Value="PROP_CO_4" />
        <PropertyID Value="PolytropicEfficiency" />
        <PropertyID Value="AdiabaticCoefficient" />
        <PropertyID Value="PolytropicCoefficient" />
        <PropertyID Value="AdiabaticHead" />
        <PropertyID Value="PolytropicHead" />
        <PropertyID Value="RotationSpeed" />
      </ObjectType>
      <ObjectType Value="Cooler">
        <PropertyID Value="Flow Conductance" />
        <PropertyID Value="Volume" />
        <PropertyID Value="Minimum Pressure" />
        <PropertyID Value="Initialize using Inlet Stream" />
        <PropertyID Value="Reset Content" />
        <PropertyID Value="PROP_CL_0" />
        <PropertyID Value="PROP_CL_1" />
        <PropertyID Value="PROP_CL_2" />
        <PropertyID Value="PROP_CL_3" />
        <PropertyID Value="PROP_CL_4" />
        <PropertyID Value="PROP_CL_5" />
      </ObjectType>
      <ObjectType Value="CustomUO" />
      <ObjectType Value="DigitalGauge" />
      <ObjectType Value="DistillationColumn">
        <PropertyID Value="PROP_DC_0" />
        <PropertyID Value="PROP_DC_1" />
        <PropertyID Value="PROP_DC_2" />
        <PropertyID Value="PROP_DC_3" />
        <PropertyID Value="PROP_DC_4" />
        <PropertyID Value="PROP_DC_5" />
        <PropertyID Value="PROP_DC_6" />
        <PropertyID Value="PROP_DC_7" />
        <PropertyID Value="Condenser_Specification_Value" />
        <PropertyID Value="Reboiler_Specification_Value" />
        <PropertyID Value="Global_Stage_Efficiency" />
      </ObjectType>
      <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" />
      </ObjectType>
      <ObjectType Value="Input" />
      <ObjectType Value="LevelGauge" />
      <ObjectType Value="MaterialStream">
        <PropertyID Value="PROP_MS_0" />
        <PropertyID Value="PROP_MS_1" />
        <PropertyID Value="PROP_MS_2" />
        <PropertyID Value="PROP_MS_3" />
        <PropertyID Value="PROP_MS_4" />
        <PropertyID Value="PROP_MS_9" />
        <PropertyID Value="PROP_MS_10" />
        <PropertyID Value="PROP_MS_27" />
        <PropertyID Value="PROP_MS_130" />
        <PropertyID Value="PROP_MS_154" />
      </ObjectType>
      <ObjectType Value="Mixer" />
      <ObjectType Value="OrificePlate">
        <PropertyID Value="PROP_OP_0" />
        <PropertyID Value="PROP_OP_1" />
        <PropertyID Value="PROP_OP_2" />
        <PropertyID Value="PROP_OP_3" />
        <PropertyID Value="PROP_OP_4" />
        <PropertyID Value="PROP_OP_5" />
        <PropertyID Value="PROP_OP_6" />
        <PropertyID Value="PROP_OP_7" />
      </ObjectType>
      <ObjectType Value="PIDController">
        <PropertyID Value="Active" />
        <PropertyID Value="ManualOverride" />
        <PropertyID Value="LastError" />
        <PropertyID Value="CurrentError" />
        <PropertyID Value="CumulativeError" />
        <PropertyID Value="SetPoint" />
        <PropertyID Value="SetPointAbs" />
        <PropertyID Value="Kp" />
        <PropertyID Value="Ki" />
        <PropertyID Value="Kd" />
        <PropertyID Value="Output" />
        <PropertyID Value="OutputMin" />
        <PropertyID Value="OutputMax" />
        <PropertyID Value="OutputAbs" />
      </ObjectType>
      <ObjectType Value="Pipe">
        <PropertyID Value="PROP_PS_0" />
        <PropertyID Value="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" />
      </ObjectType>
      <ObjectType Value="Reactor_Conversion">
        <PropertyID Value="PROP_CR_0" />
        <PropertyID Value="Calculation Mode" />
      </ObjectType>
      <ObjectType Value="Reactor_CSTR">
        <PropertyID Value="Operating Pressure" />
        <PropertyID Value="Liquid Level" />
        <PropertyID Value="Height" />
        <PropertyID Value="Minimum Pressure" />
        <PropertyID Value="Initialize using Inlet Stream" />
        <PropertyID Value="Reset Contents" />
        <PropertyID Value="PROP_CS_0" />
        <PropertyID Value="PROP_CS_1" />
        <PropertyID Value="PROP_CS_2" />
        <PropertyID Value="PROP_CS_3" />
        <PropertyID Value="PROP_CS_4" />
        <PropertyID Value="PROP_CS_5" />
        <PropertyID Value="Calculation Mode" />
      </ObjectType>
      <ObjectType Value="Reactor_Equilibrium">
        <PropertyID Value="PROP_EQ_0" />
        <PropertyID Value="Calculation Mode" />
        <PropertyID Value="Initial Gibbs Energy" />
        <PropertyID Value="Final Gibbs Energy" />
      </ObjectType>
      <ObjectType Value="Reactor_Gibbs">
        <PropertyID Value="PROP_GR_0" />
        <PropertyID Value="PROP_GR_1" />
        <PropertyID Value="Calculation Mode" />
        <PropertyID Value="Initial Gibbs Energy" />
        <PropertyID Value="Final Gibbs Energy" />
        <PropertyID Value="Element Balance Residue" />
      </ObjectType>
      <ObjectType Value="Reactor_PFR">
        <PropertyID Value="Max Sections" />
        <PropertyID Value="Reset Contents" />
        <PropertyID Value="PROP_PF_0" />
        <PropertyID Value="PROP_PF_1" />
        <PropertyID Value="PROP_PF_2" />
        <PropertyID Value="PROP_PF_3" />
        <PropertyID Value="PROP_PF_4" />
        <PropertyID Value="PROP_PF_5" />
        <PropertyID Value="PROP_PF_6" />
        <PropertyID Value="PROP_PF_7" />
        <PropertyID Value="PROP_PF_8" />
        <PropertyID Value="Calculation Mode" />
      </ObjectType>
      <ObjectType Value="ReboiledAbsorber">
        <PropertyID Value="PROP_RA_0" />
        <PropertyID Value="PROP_RA_1" />
        <PropertyID Value="PROP_RA_2" />
        <PropertyID Value="PROP_RA_3" />
        <PropertyID Value="PROP_RA_4" />
      </ObjectType>
      <ObjectType Value="Recycle">
        <PropertyID Value="PROP_RY_0" />
        <PropertyID Value="PROP_RY_1" />
        <PropertyID Value="PROP_RY_2" />
        <PropertyID Value="PROP_RY_3" />
        <PropertyID Value="PROP_RY_4" />
        <PropertyID Value="PROP_RY_5" />
        <PropertyID Value="PROP_RY_6" />
      </ObjectType>
      <ObjectType Value="RefluxedAbsorber">
        <PropertyID Value="PROP_RF_0" />
        <PropertyID Value="PROP_RF_1" />
        <PropertyID Value="PROP_RF_2" />
        <PropertyID Value="PROP_RF_3" />
        <PropertyID Value="PROP_RF_4" />
        <PropertyID Value="PROP_RF_5" />
        <PropertyID Value="PROP_RF_6" />
      </ObjectType>
      <ObjectType Value="ShortcutColumn">
        <PropertyID Value="PROP_SC_0" />
        <PropertyID Value="PROP_SC_1" />
        <PropertyID Value="PROP_SC_2" />
        <PropertyID Value="PROP_SC_3" />
        <PropertyID Value="PROP_SC_4" />
        <PropertyID Value="PROP_SC_5" />
        <PropertyID Value="PROP_SC_6" />
        <PropertyID Value="PROP_SC_7" />
        <PropertyID Value="PROP_SC_8" />
        <PropertyID Value="PROP_SC_9" />
        <PropertyID Value="PROP_SC_10" />
        <PropertyID Value="PROP_SC_11" />
        <PropertyID Value="PROP_SC_12" />
        <PropertyID Value="PROP_SC_13" />
        <PropertyID Value="PROP_SC_14" />
      </ObjectType>
      <ObjectType Value="SolidsSeparator">
        <PropertyID Value="PROP_SS_1" />
        <PropertyID Value="PROP_SS_2" />
      </ObjectType>
      <ObjectType Value="Spec">
        <PropertyID Value="SpecMin" />
        <PropertyID Value="SpecMax" />
        <PropertyID Value="Expression" />
      </ObjectType>
      <ObjectType Value="Splitter">
        <PropertyID Value="PROP_SP_1" />
        <PropertyID Value="PROP_SP_2" />
      </ObjectType>
      <ObjectType Value="Switch" />
      <ObjectType Value="Tank">
        <PropertyID Value="Liquid Level" />
        <PropertyID Value="Height" />
        <PropertyID Value="Initialize using Inlet Stream" />
        <PropertyID Value="Reset Content" />
        <PropertyID Value="PROP_TK_0" />
        <PropertyID Value="PROP_TK_1" />
        <PropertyID Value="PROP_TK_2" />
      </ObjectType>
      <ObjectType Value="Valve">
        <PropertyID Value="PROP_VA_0" />
        <PropertyID Value="PROP_VA_1" />
        <PropertyID Value="PROP_VA_2" />
        <PropertyID Value="PROP_VA_3" />
        <PropertyID Value="PROP_VA_4" />
        <PropertyID Value="PROP_VA_5" />
      </ObjectType>
      <ObjectType Value="Vessel">
        <PropertyID Value="Vessel Orientation" />
        <PropertyID Value="Operating Pressure" />
        <PropertyID Value="Liquid Level" />
        <PropertyID Value="Volume" />
        <PropertyID Value="Height" />
        <PropertyID Value="Minimum Pressure" />
        <PropertyID Value="Initialize using Inlet Stream" />
        <PropertyID Value="Reset Content" />
        <PropertyID Value="PROP_SV_0" />
        <PropertyID Value="PROP_SV_1" />
      </ObjectType>
    </VisibleProperties>
    <FlashAlgorithms>
      <FlashAlgorithm>
        <ID>Nested Loops (VLE) (1)</ID>
        <Type>DWSIM.Thermodynamics.PropertyPackages.Auxiliary.FlashAlgorithms.NestedLoops</Type>
        <LimitVaporFraction>true</LimitVaporFraction>
        <AlgoType>Nested_Loops_VLE</AlgoType>
        <Description>Flash Algorithm for Vapor-Liquid Equilibria based on the Rachford-Rice VLE equations.</Description>
        <Name>Nested Loops (VLE)</Name>
        <MobileCompatible>true</MobileCompatible>
        <Order>1</Order>
        <StabSearchSeverity>0</StabSearchSeverity>
        <InternalUseOnly>false</InternalUseOnly>
        <Tag>Nested Loops (VLE) (1)</Tag>
        <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" />
          <Setting Name="PVFlash_MaximumTemperatureChange" Value="10" />
          <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" />
        </FlashSettings>
      </FlashAlgorithm>
    </FlashAlgorithms>
  </Settings>
  <DynamicProperties />
  <GraphicObjects>
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      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
      <SemiTransparent>false</SemiTransparent>
      <LineWidth>1</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>#ff4682b4</LineColor>
      <LineColorDark>#fff5f5f5</LineColorDark>
      <Fill>false</Fill>
      <FillColor>#ffffffff</FillColor>
      <FillColorDark>#ffffffff</FillColorDark>
      <GradientColor1>#ffd3d3d3</GradientColor1>
      <GradientColor2>#ffffffff</GradientColor2>
      <FontSize>10</FontSize>
      <OverrideColors>false</OverrideColors>
      <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-01254e59-219d-42a7-bf1a-a576a81ca37f</Name>
      <Tag>Biogas Feed</Tag>
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      <X>928</X>
      <Y>442</Y>
      <Selected>false</Selected>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="false" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="COMP-16912814-94f1-4d57-b70b-9175d491ce81" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
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      <EnergyConnector>
        <Connector IsAttached="false" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CompressorGraphic</Type>
      <SemiTransparent>false</SemiTransparent>
      <LineWidth>1</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>#ff4682b4</LineColor>
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      <FontSize>10</FontSize>
      <OverrideColors>false</OverrideColors>
      <Calculated>true</Calculated>
      <Active>true</Active>
      <Description>Adiabatic Compressor</Description>
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      <FlippedV>false</FlippedV>
      <IsEnergyStream>false</IsEnergyStream>
      <ObjectType>Compressor</ObjectType>
      <Shape>0</Shape>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <AutoSize>false</AutoSize>
      <Height>25</Height>
      <IsConnector>false</IsConnector>
      <Name>COMP-16912814-94f1-4d57-b70b-9175d491ce81</Name>
      <Tag>compressor1</Tag>
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      <Y>440</Y>
      <Selected>false</Selected>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-01254e59-219d-42a7-bf1a-a576a81ca37f" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
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      <EnergyConnector>
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      <SpecialConnectors />
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    <GraphicObject>
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      <GradientMode>true</GradientMode>
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      <Active>true</Active>
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      <ObjectType>EnergyStream</ObjectType>
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      <IsConnector>false</IsConnector>
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      <Selected>false</Selected>
      <Rotation>0</Rotation>
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      <EnergyConnector>
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      <SpecialConnectors />
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    <GraphicObject>
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Pressure	200	kPa
Volumetric Flow	1500	m3/h
Molar Fraction (Mixture)  /  Methane	0.6	
Molar Fraction (Mixture)  /  Carbon dioxide	0.4	
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Liquid CO2	Pressure	2620	kPa
Liquid CO2	Volumetric Flow	1.74817	m3/h
Liquid CO2	Mass Flow	2074.3	kg/h
Liquid CO2	Molar Fraction (Mixture) / Methane	0.002	
Liquid CO2	Molar Fraction (Mixture) / Carbon dioxide	0.998	
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Liquefied Biomethane	Pressure	100	kPa
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      <Height>30</Height>
      <IsConnector>false</IsConnector>
      <Name>HE-e5c9c402-5591-4f01-9b82-02d178bab24d</Name>
      <Tag>HE-021</Tag>
      <Width>30</Width>
      <X>1286</X>
      <Y>372</Y>
      <Selected>false</Selected>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-fc159a44-1084-409b-a887-8e2699abbc9e" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
        <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-9edbfbc0-df95-45d2-bbe3-50d8eac70c8a" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-d5d9bba1-3bae-4a1e-a5a7-c89e7151e1db" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
        <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-3ffacbf8-9159-4c5a-9ff0-321d629e3250" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="false" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
  </GraphicObjects>
  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-f1a6f133-8bcd-4b3c-8b15-f568d76417f1</ID>
      <Type>DWSIM.Thermodynamics.PropertyPackages.PengRobinsonPropertyPackage</Type>
      <ComponentName>Peng-Robinson (PR)</ComponentName>
      <ComponentDescription>Property Package that uses the Peng-Robinson Cubic Equation of State. Recommended for use with hydrocarbons and non-condensables.</ComponentDescription>
      <Tag>Peng-Robinson (PR) (1)</Tag>
      <TPSeverity>0</TPSeverity>
      <TPCompIDs></TPCompIDs>
      <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
      <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
      <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
      <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
      <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
      <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
      <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
      <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
      <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
      <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
      <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
      <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
      <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
      <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
      <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
      <EnthalpyEntropyCpCvCalculationMode>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
      <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
      <ActivityCoefficientModels_IgnoreMissingInteractionParameters>true</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
      <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
      <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
      <ForcedSolids>[]</ForcedSolids>
      <PropertyOverrides>{}</PropertyOverrides>
      <InteractionParameters>
        <InteractionParameter Compound1="Nitrogen" Compound2="Methane" Value="0.0289" />
        <InteractionParameter Compound1="Nitrogen" Compound2="Carbon dioxide" Value="-0.0222" />
        <InteractionParameter Compound1="Methane" Compound2="Carbon dioxide" Value="0.0793" />
      </InteractionParameters>
    </PropertyPackage>
  </PropertyPackages>
  <Compounds>
    <Compound>
      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
      <Acentric_Factor>0.011</Acentric_Factor>
      <BO_BSW>0</BO_BSW>
      <BO_GOR>0</BO_GOR>
      <BO_OilVisc1>0</BO_OilVisc1>
      <BO_OilVisc2>0</BO_OilVisc2>
      <BO_OilViscTemp1>0</BO_OilViscTemp1>
      <BO_OilViscTemp2>0</BO_OilViscTemp2>
      <BO_PNA_A>0</BO_PNA_A>
      <BO_PNA_N>0</BO_PNA_N>
      <BO_PNA_P>0</BO_PNA_P>
      <BO_SGG>0</BO_SGG>
      <BO_SGO>0</BO_SGO>
      <CAS_Number>74-82-8</CAS_Number>
      <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
      <Chao_Seader_Liquid_Molar_Volume>37.8392</Chao_Seader_Liquid_Molar_Volume>
      <Chao_Seader_Solubility_Parameter>0.00277501792024</Chao_Seader_Solubility_Parameter>
      <Charge>0</Charge>
      <ChemicalStructure></ChemicalStructure>
      <Comments></Comments>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <Critical_Compressibility>0.286</Critical_Compressibility>
      <Critical_Pressure>4599000</Critical_Pressure>
      <Critical_Temperature>190.56</Critical_Temperature>
      <Critical_Volume>0.0986</Critical_Volume>
      <CurrentDB>ChemSep</CurrentDB>
      <Dipole_Moment>0</Dipole_Moment>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <EnthalpyOfFusionAtTf>0.9414</EnthalpyOfFusionAtTf>
      <Formula>CH4</Formula>
      <HVap_A>14418000</HVap_A>
      <HVap_B>2.3055</HVap_B>
      <HVap_C>-5.4199</HVap_C>
      <HVap_D>5.658</HVap_D>
      <HVap_E>-2.1286</HVap_E>
      <HVap_TMAX>190.55</HVap_TMAX>
      <HVap_TMIN>90.67</HVap_TMIN>
      <HydrationNumber>0</HydrationNumber>
      <ID>1</ID>
      <Ideal_Gas_Heat_Capacity_Const_A>33151.9</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-1220.001</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>12.0907</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.000384791</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>9.896403E-08</Ideal_Gas_Heat_Capacity_Const_E>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <IG_Enthalpy_of_Formation_25C>-4645.17287248963</IG_Enthalpy_of_Formation_25C>
      <IG_Entropy_of_Formation_25C>11.6110621438358</IG_Entropy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-3147.27292447667</IG_Gibbs_Energy_of_Formation_25C>
      <InChI></InChI>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <IsBlackOil>false</IsBlackOil>
      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsHydratedSalt>false</IsHydratedSalt>
      <IsHYPO>0</IsHYPO>
      <IsIon>false</IsIon>
      <IsModified>false</IsModified>
      <IsPF>0</IsPF>
      <IsSalt>false</IsSalt>
      <Liquid_Density_Const_A>1.894</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.23603</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>191.05</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.21974</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmax>191.04</Liquid_Density_Tmax>
      <Liquid_Density_Tmin>90.68</Liquid_Density_Tmin>
      <Liquid_Heat_Capacity_Const_A>61157</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>5034.1</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>-48.913</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-0.22998</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.0022243</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmax>190</Liquid_Heat_Capacity_Tmax>
      <Liquid_Heat_Capacity_Tmin>88.71</Liquid_Heat_Capacity_Tmin>
      <Liquid_Thermal_Conductivity_Const_A>0.011567</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-46.041</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0.10435</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.012133</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-5.1716E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmax>180</Liquid_Thermal_Conductivity_Tmax>
      <Liquid_Thermal_Conductivity_Tmin>90.69</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Viscosity_Const_A>-45.328</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>724.39</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>6.5917</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-0.00010373</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <Molar_Weight>16.04246</Molar_Weight>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <Name>Methane</Name>
      <NegativeIon></NegativeIon>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <Normal_Boiling_Point>111.66</Normal_Boiling_Point>
      <OriginalDB>ChemSep</OriginalDB>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PositiveIon></PositiveIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SMILES>C</SMILES>
      <Solid_Density_Const_A>33.457</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.033547</Solid_Density_Const_B>
      <Solid_Density_Const_C>-0.000155</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmax>90.69</Solid_Density_Tmax>
      <Solid_Density_Tmin>23.15</Solid_Density_Tmin>
      <Solid_Heat_Capacity_Const_A>-3039.8</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>1292.4</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>-15.448</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0.082442</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>-7.0636E-05</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmax>90.67</Solid_Heat_Capacity_Tmax>
      <Solid_Heat_Capacity_Tmin>22.85</Solid_Heat_Capacity_Tmin>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <SolidDensityEquation>2</SolidDensityEquation>
      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
      <SolidTs>0</SolidTs>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <StoichSum>0</StoichSum>
      <Surface_Tension_Const_A>-0.040703</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>-6.9523</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-2.3114</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>-0.0055565</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>5.7595E-06</Surface_Tension_Const_E>
      <Surface_Tension_Tmax>193.15</Surface_Tension_Tmax>
      <Surface_Tension_Tmin>90</Surface_Tension_Tmin>
      <SurfaceTensionEquation>16</SurfaceTensionEquation>
      <TemperatureOfFusion>90.694</TemperatureOfFusion>
      <UNIQUAC_Q>1.152</UNIQUAC_Q>
      <UNIQUAC_R>1.1239</UNIQUAC_R>
      <Vapor_Pressure_Constant_A>39.98844</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-1337.308</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-3.580049</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>3.20698E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMAX>191.03</Vapor_Pressure_TMAX>
      <Vapor_Pressure_TMIN>83.65</Vapor_Pressure_TMIN>
      <Vapor_Thermal_Conductivity_Const_A>7.4705E-06</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>1.4432</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>-57.569</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>587.82</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmax>600</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Tmin>90.694</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Viscosity_Const_A>5.3432E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.58831</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>114.58</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>-1338.5</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
      <Vapor_Viscosity_Tmin>90</Vapor_Viscosity_Tmin>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <VaporPressureEquation>101</VaporPressureEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <Z_Rackett>0.2876</Z_Rackett>
      <FullerDiffusionVolume>25.14</FullerDiffusionVolume>
      <LennardJonesDiameter>3.871667E-10</LennardJonesDiameter>
      <LennardJonesEnergy>137.3608</LennardJonesEnergy>
      <Parachor>0.0129</Parachor>
      <Tag></Tag>
      <DynamicProperties />
      <UNIFACGroups />
      <MODFACGroups />
      <NISTMODFACGroups />
      <Elements />
    </Compound>
    <Compound>
      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
      <Acentric_Factor>0.223621</Acentric_Factor>
      <BO_BSW>0</BO_BSW>
      <BO_GOR>0</BO_GOR>
      <BO_OilVisc1>0</BO_OilVisc1>
      <BO_OilVisc2>0</BO_OilVisc2>
      <BO_OilViscTemp1>0</BO_OilViscTemp1>
      <BO_OilViscTemp2>0</BO_OilViscTemp2>
      <BO_PNA_A>0</BO_PNA_A>
      <BO_PNA_N>0</BO_PNA_N>
      <BO_PNA_P>0</BO_PNA_P>
      <BO_SGG>0</BO_SGG>
      <BO_SGO>0</BO_SGO>
      <CAS_Number>124-38-9</CAS_Number>
      <Chao_Seader_Acentricity>0.231</Chao_Seader_Acentricity>
      <Chao_Seader_Liquid_Molar_Volume>37.2744</Chao_Seader_Liquid_Molar_Volume>
      <Chao_Seader_Solubility_Parameter>0.0034785053748</Chao_Seader_Solubility_Parameter>
      <Charge>0</Charge>
      <ChemicalStructure></ChemicalStructure>
      <Comments></Comments>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <Critical_Compressibility>0.274</Critical_Compressibility>
      <Critical_Pressure>7383000</Critical_Pressure>
      <Critical_Temperature>304.21</Critical_Temperature>
      <Critical_Volume>0.094</Critical_Volume>
      <CurrentDB>ChemSep</CurrentDB>
      <Dipole_Moment>0</Dipole_Moment>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <EnthalpyOfFusionAtTf>9.019</EnthalpyOfFusionAtTf>
      <Formula>CO2</Formula>
      <HVap_A>21092000</HVap_A>
      <HVap_B>0.35366</HVap_B>
      <HVap_C>-0.46134</HVap_C>
      <HVap_D>0.43554</HVap_D>
      <HVap_E>0.037671</HVap_E>
      <HVap_TMAX>304.21</HVap_TMAX>
      <HVap_TMIN>216.58</HVap_TMIN>
      <HydrationNumber>0</HydrationNumber>
      <ID>909</ID>
      <Ideal_Gas_Heat_Capacity_Const_A>28933</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-494.28</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>10.658</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-2.7375E-05</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>3.3268E-09</Ideal_Gas_Heat_Capacity_Const_E>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <IG_Enthalpy_of_Formation_25C>-8941.47854440518</IG_Enthalpy_of_Formation_25C>
      <IG_Entropy_of_Formation_25C>4.85524716254445</IG_Entropy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-8961.01977982027</IG_Gibbs_Energy_of_Formation_25C>
      <InChI></InChI>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <IsBlackOil>false</IsBlackOil>
      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsHydratedSalt>false</IsHydratedSalt>
      <IsHYPO>0</IsHYPO>
      <IsIon>false</IsIon>
      <IsModified>false</IsModified>
      <IsPF>0</IsPF>
      <IsSalt>false</IsSalt>
      <Liquid_Density_Const_A>2.768</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.26212</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>304.21</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.2908</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmax>304.21</Liquid_Density_Tmax>
      <Liquid_Density_Tmin>216.58</Liquid_Density_Tmin>
      <Liquid_Heat_Capacity_Const_A>80592</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>108.83</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>-6.9126</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0.059647</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>6.9922E-06</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmax>290</Liquid_Heat_Capacity_Tmax>
      <Liquid_Heat_Capacity_Tmin>216.58</Liquid_Heat_Capacity_Tmin>
      <Liquid_Thermal_Conductivity_Const_A>-0.24975</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-55.106</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0.41735</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.0051067</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>2.0157E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmax>300</Liquid_Thermal_Conductivity_Tmax>
      <Liquid_Thermal_Conductivity_Tmin>216.58</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Viscosity_Const_A>-7.7022</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>-166.34</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>0.38094</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-4.018E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <Molar_Weight>44.0095</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>Carbon dioxide</Name>
      <NegativeIon></NegativeIon>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <Normal_Boiling_Point>0</Normal_Boiling_Point>
      <OriginalDB>ChemSep</OriginalDB>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PositiveIon></PositiveIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SMILES>O=C=O</SMILES>
      <Solid_Density_Const_A>42.04</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.034421</Solid_Density_Const_B>
      <Solid_Density_Const_C>-0.0002847</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmax>216.58</Solid_Density_Tmax>
      <Solid_Density_Tmin>143.1</Solid_Density_Tmin>
      <Solid_Heat_Capacity_Const_A>-18283</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>1360.3</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>-12.153</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0.051584</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>-7.6997E-05</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmax>216.58</Solid_Heat_Capacity_Tmax>
      <Solid_Heat_Capacity_Tmin>25</Solid_Heat_Capacity_Tmin>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <SolidDensityEquation>2</SolidDensityEquation>
      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
      <SolidTs>0</SolidTs>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <StoichSum>0</StoichSum>
      <Surface_Tension_Const_A>-0.011629</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>-183.67</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0.069773</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>-0.012408</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-1.8232E-06</Surface_Tension_Const_E>
      <Surface_Tension_Tmax>304.21</Surface_Tension_Tmax>
      <Surface_Tension_Tmin>216.58</Surface_Tension_Tmin>
      <SurfaceTensionEquation>16</SurfaceTensionEquation>
      <TemperatureOfFusion>216.58</TemperatureOfFusion>
      <UNIQUAC_Q>1.292</UNIQUAC_Q>
      <UNIQUAC_R>1.2986</UNIQUAC_R>
      <Vapor_Pressure_Constant_A>95.478</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-4070</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-12.07</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>2.9505E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMAX>304.21</Vapor_Pressure_TMAX>
      <Vapor_Pressure_TMIN>216.4</Vapor_Pressure_TMIN>
      <Vapor_Thermal_Conductivity_Const_A>5.804</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>-0.44522</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>794.13</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>2139600</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmax>1500</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Tmin>180</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Viscosity_Const_A>2.2464E-06</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.45495</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>292.64</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>1669.1</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmax>1900</Vapor_Viscosity_Tmax>
      <Vapor_Viscosity_Tmin>170</Vapor_Viscosity_Tmin>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <VaporPressureEquation>101</VaporPressureEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <Z_Rackett>0.270937</Z_Rackett>
      <FullerDiffusionVolume>26.9</FullerDiffusionVolume>
      <LennardJonesDiameter>4.011624E-10</LennardJonesDiameter>
      <LennardJonesEnergy>187.9268</LennardJonesEnergy>
      <Parachor>0.0132</Parachor>
      <Tag></Tag>
      <DynamicProperties />
      <UNIFACGroups />
      <MODFACGroups />
      <NISTMODFACGroups />
      <Elements />
    </Compound>
    <Compound>
      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
      <Acentric_Factor>0.037</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>7727-37-9</CAS_Number>
      <Chao_Seader_Acentricity>0.045</Chao_Seader_Acentricity>
      <Chao_Seader_Liquid_Molar_Volume>34.6723</Chao_Seader_Liquid_Molar_Volume>
      <Chao_Seader_Solubility_Parameter>0.00216918504124</Chao_Seader_Solubility_Parameter>
      <Charge>0</Charge>
      <ChemicalStructure></ChemicalStructure>
      <Comments></Comments>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <Critical_Compressibility>0.289</Critical_Compressibility>
      <Critical_Pressure>3398000</Critical_Pressure>
      <Critical_Temperature>126.2</Critical_Temperature>
      <Critical_Volume>0.0901</Critical_Volume>
      <CurrentDB>ChemSep</CurrentDB>
      <Dipole_Moment>0</Dipole_Moment>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <EnthalpyOfFusionAtTf>0.72</EnthalpyOfFusionAtTf>
      <Formula>N2</Formula>
      <HVap_A>27284000</HVap_A>
      <HVap_B>7.8021</HVap_B>
      <HVap_C>-19.125</HVap_C>
      <HVap_D>19.518</HVap_D>
      <HVap_E>-7.5428</HVap_E>
      <HVap_TMAX>126.26</HVap_TMAX>
      <HVap_TMIN>63.15</HVap_TMIN>
      <HydrationNumber>0</HydrationNumber>
      <ID>905</ID>
      <Ideal_Gas_Heat_Capacity_Const_A>29103.63</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-2305.946</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>11.31935</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.00100557</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.706099E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <IG_Enthalpy_of_Formation_25C>0</IG_Enthalpy_of_Formation_25C>
      <IG_Entropy_of_Formation_25C>6.83601419320754</IG_Entropy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>0</IG_Gibbs_Energy_of_Formation_25C>
      <InChI></InChI>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <IsBlackOil>false</IsBlackOil>
      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsHydratedSalt>false</IsHydratedSalt>
      <IsHYPO>0</IsHYPO>
      <IsIon>false</IsIon>
      <IsModified>false</IsModified>
      <IsPF>0</IsPF>
      <IsSalt>false</IsSalt>
      <Liquid_Density_Const_A>2.435</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.25137</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>126.27</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.249</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmax>126.26</Liquid_Density_Tmax>
      <Liquid_Density_Tmin>63.15</Liquid_Density_Tmin>
      <Liquid_Heat_Capacity_Const_A>55135</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>217.45</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>-0.9071</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0.05327</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.00024166</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmax>115</Liquid_Heat_Capacity_Tmax>
      <Liquid_Heat_Capacity_Tmin>63.15</Liquid_Heat_Capacity_Tmin>
      <Liquid_Thermal_Conductivity_Const_A>-0.21743</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>10.383</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-1.0631</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0.00036245</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-2.3265E-05</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmax>124</Liquid_Thermal_Conductivity_Tmax>
      <Liquid_Thermal_Conductivity_Tmin>60</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Viscosity_Const_A>3.4358</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>-24.706</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-2.6748</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-4.1603E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <Molar_Weight>28.0134</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>Nitrogen</Name>
      <NegativeIon></NegativeIon>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <Normal_Boiling_Point>77.35</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>N#N</SMILES>
      <Solid_Density_Const_A>37.87</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.06027</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>63.15</Solid_Density_Tmax>
      <Solid_Density_Tmin>20.65</Solid_Density_Tmin>
      <Solid_Heat_Capacity_Const_A>383890</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-28798</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>875.74</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-11.589</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.057106</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmax>63</Solid_Heat_Capacity_Tmax>
      <Solid_Heat_Capacity_Tmin>32.8</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>-0.0025409</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>96.836</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-7.6473</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.05313</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-0.00036553</Surface_Tension_Const_E>
      <Surface_Tension_Tmax>126.2</Surface_Tension_Tmax>
      <Surface_Tension_Tmin>63.15</Surface_Tension_Tmin>
      <SurfaceTensionEquation>16</SurfaceTensionEquation>
      <TemperatureOfFusion>63.149</TemperatureOfFusion>
      <UNIQUAC_Q>1.088</UNIQUAC_Q>
      <UNIQUAC_R>1.0415</UNIQUAC_R>
      <Vapor_Pressure_Constant_A>42.32946</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-965.9771</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-4.321774</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>7.97271E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMAX>126.26</Vapor_Pressure_TMAX>
      <Vapor_Pressure_TMIN>60.81</Vapor_Pressure_TMIN>
      <Vapor_Thermal_Conductivity_Const_A>0.0003395</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.76921</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>19.592</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>293.93</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmax>2000</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Tmin>50</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Viscosity_Const_A>4.6051E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.65049</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>5.8019</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>2822.7</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmax>1970</Vapor_Viscosity_Tmax>
      <Vapor_Viscosity_Tmin>63.15</Vapor_Viscosity_Tmin>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <VaporPressureEquation>101</VaporPressureEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <Z_Rackett>0.2906</Z_Rackett>
      <FullerDiffusionVolume>18.5</FullerDiffusionVolume>
      <LennardJonesDiameter>3.710301E-10</LennardJonesDiameter>
      <LennardJonesEnergy>94.45061</LennardJonesEnergy>
      <Parachor>0.0107</Parachor>
      <Tag></Tag>
      <DynamicProperties />
      <UNIFACGroups />
      <MODFACGroups />
      <NISTMODFACGroups />
      <Elements />
    </Compound>
  </Compounds>
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    <ReactionSet>
      <ID>DefaultSet</ID>
      <Name>Default Set</Name>
      <Description>Default Reaction Set</Description>
      <Reactions />
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  </ReactionSets>
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    <Type>DWSIM.DynamicsManager.Manager</Type>
    <Description></Description>
    <CurrentSchedule></CurrentSchedule>
    <ScheduleList />
    <EventSetList />
    <IntegratorList />
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  <OptimizationCases />
  <SensitivityAnalysis />
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&lt;!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.--&gt;
&lt;!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!--&gt;
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    &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="3"&gt;
      &lt;NestedPanes Count="1"&gt;
        &lt;Pane ID="0" RefID="3" PrevPane="-1" Alignment="Bottom" Proportion="0.5" /&gt;
      &lt;/NestedPanes&gt;
    &lt;/DockWindow&gt;
    &lt;DockWindow ID="2" DockState="DockRight" ZOrderIndex="4"&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="2"&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="5" 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="2"&gt;
    &lt;FloatWindow ID="0" Bounds="336, 370, 900, 155" ZOrderIndex="0"&gt;
      &lt;NestedPanes Count="1"&gt;
        &lt;Pane ID="0" RefID="4" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
      &lt;/NestedPanes&gt;
    &lt;/FloatWindow&gt;
    &lt;FloatWindow ID="1" Bounds="104, 104, 900, 600" ZOrderIndex="1"&gt;
      &lt;NestedPanes Count="1"&gt;
        &lt;Pane ID="0" RefID="6" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
      &lt;/NestedPanes&gt;
    &lt;/FloatWindow&gt;
  &lt;/FloatWindows&gt;
&lt;/DockPanel&gt;</PanelLayout>
</DWSIM_Simulation_Data>