<?xml version="1.0" encoding="utf-8"?>
<DWSIM_Simulation_Data>
  <GeneralInfo>
    <BuildVersion>3.2.5398.28421</BuildVersion>
    <BuildDate>2014-10-12T15:47:22</BuildDate>
    <OSInfo>Microsoft Windows 8 Single Language, Version 6.2.9200.0, Win32NT Platform</OSInfo>
    <SavedOn>2014-12-10T16:35:17.9394123-08:00</SavedOn>
  </GeneralInfo>
  <Settings>
    <Type>DWSIM.DWSIM.FormClasses.ClsFormOptions</Type>
    <SimulationMode></SimulationMode>
    <SelectedUnitSystem>
      <Type>DWSIM.DWSIM.SistemasDeUnidades.UnidadesSI</Type>
      <nome>SI System</nome>
      <area>m2</area>
      <distance>m</distance>
      <time>s</time>
      <volume>m3</volume>
      <molar_volume>m3/kmol</molar_volume>
      <diameter>mm</diameter>
      <thickness>mm</thickness>
      <molar_conc>mol/m3</molar_conc>
      <mass_conc>kg/m3</mass_conc>
      <heat_transf_coeff>W/[m2.K]</heat_transf_coeff>
      <force>N</force>
      <accel>m2/s</accel>
      <spec_vol>m3/kg</spec_vol>
      <reac_rate>mol/[m3.s]</reac_rate>
      <velocity>m/s</velocity>
      <foulingfactor>K.m2/W</foulingfactor>
      <cakeresistance>m/kg</cakeresistance>
      <mediumresistance>m-1</mediumresistance>
      <molar_enthalpy>kJ/kmol</molar_enthalpy>
      <molar_entropy>kJ/[kmol.K]</molar_entropy>
      <tdp_idealGasHeatCapacity>kJ/[kg.K]</tdp_idealGasHeatCapacity>
      <tdp_surfaceTension>N/m</tdp_surfaceTension>
      <tdp_thermalConductivityOfLiquid>W/[m.K]</tdp_thermalConductivityOfLiquid>
      <tdp_thermalConductivityOfVapor>W/[m.K]</tdp_thermalConductivityOfVapor>
      <tdp_vaporPressure>Pa</tdp_vaporPressure>
      <tdp_viscosityOfLiquid>Pa.s</tdp_viscosityOfLiquid>
      <tdp_viscosityOfVapor>Pa.s</tdp_viscosityOfVapor>
      <pdp_boilingPointTemperature>K</pdp_boilingPointTemperature>
      <pdp_meltingTemperature>K</pdp_meltingTemperature>
      <spmp_activity>Pa</spmp_activity>
      <spmp_activityCoefficient>-</spmp_activityCoefficient>
      <spmp_compressibility>Pa-1</spmp_compressibility>
      <spmp_compressibilityFactor>-</spmp_compressibilityFactor>
      <spmp_density>kg/m3</spmp_density>
      <spmp_enthalpy>kJ/kg</spmp_enthalpy>
      <spmp_entropy>kJ/[kg.K]</spmp_entropy>
      <spmp_excessEnthalpy>kJ/kg</spmp_excessEnthalpy>
      <spmp_excessEntropy>kJ/[kg.K]</spmp_excessEntropy>
      <spmp_molarflow>mol/s</spmp_molarflow>
      <spmp_massflow>kg/s</spmp_massflow>
      <spmp_molarfraction>-</spmp_molarfraction>
      <spmp_massfraction>-</spmp_massfraction>
      <spmp_fugacity>Pa</spmp_fugacity>
      <spmp_fugacityCoefficient>-</spmp_fugacityCoefficient>
      <spmp_heatCapacityCp>kJ/[kg.K]</spmp_heatCapacityCp>
      <spmp_heatCapacityCv>kJ/[kg.K]</spmp_heatCapacityCv>
      <spmp_jouleThomsonCoefficient>K/Pa</spmp_jouleThomsonCoefficient>
      <spmp_logFugacityCoefficient>-</spmp_logFugacityCoefficient>
      <spmp_molecularWeight>kg/kmol</spmp_molecularWeight>
      <spmp_pressure>Pa</spmp_pressure>
      <spmp_temperature>K</spmp_temperature>
      <spmp_speedOfSound>m/s</spmp_speedOfSound>
      <spmp_thermalConductivity>W/[m.K]</spmp_thermalConductivity>
      <spmp_viscosity>Pa.s</spmp_viscosity>
      <spmp_cinematic_viscosity>m2/s</spmp_cinematic_viscosity>
      <spmp_volumetricFlow>m3/s</spmp_volumetricFlow>
      <spmp_heatflow>kW</spmp_heatflow>
      <spmp_head>m</spmp_head>
      <spmp_deltaT>K</spmp_deltaT>
      <spmp_deltaP>Pa</spmp_deltaP>
      <tpmp_kvalue>-</tpmp_kvalue>
      <tpmp_logKvalue>-</tpmp_logKvalue>
      <tpmp_surfaceTension>N/m</tpmp_surfaceTension>
    </SelectedUnitSystem>
    <NumberFormat>#0.0####</NumberFormat>
    <FractionNumberFormat>#0.0######</FractionNumberFormat>
    <SempreCalcularFlashPH>false</SempreCalcularFlashPH>
    <CalculateBubbleAndDewPoints>false</CalculateBubbleAndDewPoints>
    <ValidateEquilibriumCalc>true</ValidateEquilibriumCalc>
    <UsePhaseIdentificationAlgorithm>true</UsePhaseIdentificationAlgorithm>
    <SimNome>simulation_title</SimNome>
    <SimAutor>VAIO\tanmay.lad00</SimAutor>
    <SimComentario>simulation_details</SimComentario>
    <FilePath>F:\ex7.6.2.dwxml</FilePath>
    <BackupFileName>20187947.dwbcs</BackupFileName>
    <CalculatorActivated>true</CalculatorActivated>
    <PropertyPackageFlashAlgorithm>DWSIMDefault</PropertyPackageFlashAlgorithm>
    <PropertyPackageIOFlashQuickMode>true</PropertyPackageIOFlashQuickMode>
    <ThreePhaseFlashStabTestSeverity>0</ThreePhaseFlashStabTestSeverity>
    <FlashValidationDGETolerancePct>0.01</FlashValidationDGETolerancePct>
    <Password></Password>
    <UsePassword>false</UsePassword>
    <ThreePhaseFlashStabTestCompIds>Etano,nButano</ThreePhaseFlashStabTestCompIds>
  </Settings>
  <SimulationObjects>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.UnitOps.Heater</Type>
      <FixOnHeat>true</FixOnHeat>
      <Eficiencia>92</Eficiencia>
      <OutletTemperature>250</OutletTemperature>
      <CalcMode>OutletTemperature</CalcMode>
      <DeltaT>100</DeltaT>
      <DeltaQ>475.886828407626</DeltaQ>
      <ScriptExt_FontName>Courier New</ScriptExt_FontName>
      <ScriptExt_FontSize>10</ScriptExt_FontSize>
      <ScriptExt_ScriptTextB></ScriptExt_ScriptTextB>
      <ScriptExt_ScriptTextA></ScriptExt_ScriptTextA>
      <ScriptExt_Language>IronPython</ScriptExt_Language>
      <ErrorMessage></ErrorMessage>
      <ComponentDescription>Aquecedor</ComponentDescription>
      <ComponentName>AQ-92096e77-60c8-488f-b8ef-1d580c6715c7</ComponentName>
      <ValStatus>CAPE_VALID</ValStatus>
      <code>0</code>
      <selectedReport></selectedReport>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>Aquecedor</Descricao>
      <Nome>AQ-92096e77-60c8-488f-b8ef-1d580c6715c7</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Ethane (C2)</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-48f6141f-8248-406f-b972-58f9e9672b9d</ComponentDescription>
      <ComponentName>input</ComponentName>
      <code>0</code>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>CorrentedeMatria</Descricao>
      <Nome>MAT-48f6141f-8248-406f-b972-58f9e9672b9d</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-a26ec457-f2ab-4ba6-81a0-bb4d69a3d30b</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0.295610473662904</lnKvalue>
              <Kvalue>1.34394655228203</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.743549288087024</FracaoMolar>
              <FracaoMassica>0.6</FracaoMassica>
              <MolarFlow>19.9534419687396</MolarFlow>
              <MassFlow>0.6</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.00102429823618637</VolumetricFlow>
              <VolumetricFraction>0.645648978446002</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>-5.89013433963907</lnKvalue>
              <Kvalue>0.00276660500723096</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.256450711912976</FracaoMolar>
              <FracaoMassica>0.4</FracaoMassica>
              <MolarFlow>6.88195722863583</MolarFlow>
              <MassFlow>0.4</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.000562164796174853</VolumetricFlow>
              <VolumetricFraction>0.354351021553998</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>630.332998375413</density>
            <enthalpy>-706.996289142597</enthalpy>
            <entropy>-3.22994920709761</entropy>
            <molarflow>26.8353991973754</molarflow>
            <massflow>1</massflow>
            <heatCapacityCp>1.82438893935772</heatCapacityCp>
            <heatCapacityCv>1.41670064621054</heatCapacityCv>
            <molecularWeight>37.2642118212947</molecularWeight>
            <pressure>500000</pressure>
            <temperature>150</temperature>
            <thermalConductivity>0.12216001295868</thermalConductivity>
            <volumetric_flow>0.00158646303236122</volumetric_flow>
            <molar_enthalpy>-26345.6594754791</molar_enthalpy>
            <molar_entropy>-120.361511425308</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>0.023919417471737</surfaceTension>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>1</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.743549288087024</FracaoMolar>
              <FracaoMassica>0.6</FracaoMassica>
              <MolarFlow>19.9534419687396</MolarFlow>
              <MassFlow>0.599999999999999</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>5.13804493692822E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.256450711912976</FracaoMolar>
              <FracaoMassica>0.4</FracaoMassica>
              <MolarFlow>6.88195722863583</MolarFlow>
              <MassFlow>0.4</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>8.17600168484209E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>630.332998375413</density>
            <enthalpy>-706.996289142597</enthalpy>
            <entropy>-3.22994920709762</entropy>
            <molarflow>26.8353991973754</molarflow>
            <massflow>1</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>1.82438893935772</heatCapacityCp>
            <heatCapacityCv>1.41670064621054</heatCapacityCv>
            <molecularWeight>37.2642118212947</molecularWeight>
            <thermalConductivity>0.12216001295868</thermalConductivity>
            <viscosity>1.01055974075617E-31</viscosity>
            <kinematic_viscosity>1.60321567070221E-34</kinematic_viscosity>
            <volumetric_flow>0</volumetric_flow>
            <molar_enthalpy>-26345.6594754791</molar_enthalpy>
            <molar_entropy>-120.361511425308</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.999290502176314</FracaoMolar>
              <FracaoMassica>0.998629502352909</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.752140912842136</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.000709497823686385</FracaoMolar>
              <FracaoMassica>0.00137049764709113</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.435684727906045</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.743549288087024</FracaoMolar>
              <FracaoMassica>0.6</FracaoMassica>
              <MolarFlow>19.9534419687396</MolarFlow>
              <MassFlow>0.599999999999999</MassFlow>
              <FugacityCoeff>0.0206307099102506</FugacityCoeff>
              <ActivityCoeff>1.07234354441205</ActivityCoeff>
              <PartialVolume>5.13804493692822E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.00102429823618637</VolumetricFlow>
              <VolumetricFraction>0.645648978446002</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.256450711912976</FracaoMolar>
              <FracaoMassica>0.4</FracaoMassica>
              <MolarFlow>6.88195722863583</MolarFlow>
              <MassFlow>0.4</MassFlow>
              <FugacityCoeff>2.46009904996821E-05</FugacityCoeff>
              <ActivityCoeff>1.41474712939626</ActivityCoeff>
              <PartialVolume>8.17600168484209E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.000562164796174853</VolumetricFlow>
              <VolumetricFraction>0.354351021553998</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.0221873216890512</compressibilityFactor>
            <density>630.332998375413</density>
            <enthalpy>-706.996289142597</enthalpy>
            <entropy>-3.22994920709762</entropy>
            <molarflow>26.8353991973754</molarflow>
            <massflow>1</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>1.82438893935772</heatCapacityCp>
            <heatCapacityCv>1.41670064621054</heatCapacityCv>
            <molecularWeight>37.2642118212947</molecularWeight>
            <thermalConductivity>0.12216001295868</thermalConductivity>
            <viscosity>1.01055974075617E-31</viscosity>
            <kinematic_viscosity>1.60321567070221E-34</kinematic_viscosity>
            <volumetric_flow>0.00158646303236122</volumetric_flow>
            <molar_enthalpy>-26345.6594754791</molar_enthalpy>
            <molar_entropy>-120.361511425308</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 3</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
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              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Aqueous</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>7</ID>
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            <Compound>
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              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
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              <Kvalue>0</Kvalue>
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              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
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              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
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          <Descricao></Descricao>
          <Nome>Solid</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Ethane (C2)</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-1423c3a0-7f96-4c79-ae7c-1fecc86cf797</ComponentDescription>
      <ComponentName>output</ComponentName>
      <code>0</code>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>CorrentedeMatria</Descricao>
      <Nome>MAT-1423c3a0-7f96-4c79-ae7c-1fecc86cf797</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-a26ec457-f2ab-4ba6-81a0-bb4d69a3d30b</PropertyPackage>
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        <Phase>
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            <Compound>
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              <Nome>nButano</Nome>
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          <Descricao></Descricao>
          <Nome>Mixture</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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            <massfraction>1</massfraction>
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            <temperature>250</temperature>
            <thermalConductivity>0.0451671037314123</thermalConductivity>
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            <molar_entropy>-45.0112135002414</molar_entropy>
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          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>0.0132299397257281</surfaceTension>
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              <ActivityCoeff>NaN</ActivityCoeff>
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              <ActivityCoeff>NaN</ActivityCoeff>
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              <Nome>nButano</Nome>
            </Compound>
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          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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              <Nome>Etano</Nome>
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              <Nome>nButano</Nome>
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          <Descricao></Descricao>
          <Nome>Vapor</Nome>
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            <viscosity>8.2497676925094E-06</viscosity>
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            <molar_entropy>-22.207386836472</molar_entropy>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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            <Compound>
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              <Nome>Etano</Nome>
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              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
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          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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            <density>576.742189582749</density>
            <enthalpy>-484.358555806548</enthalpy>
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            <molarflow>9.52099401273223</molarflow>
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            <massfraction>0.45039372505278</massfraction>
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            <viscosity>2.000200978671E-32</viscosity>
            <kinematic_viscosity>3.46810241178658E-35</kinematic_viscosity>
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            <molar_entropy>-86.4811161268863</molar_entropy>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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        </Phase>
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          <ID>4</ID>
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            <Compound>
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              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
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              <Descricao></Descricao>
              <Nome>Etano</Nome>
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              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
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              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
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              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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        </Phase>
        <Phase>
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            <Compound>
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              <MolarFlow>0</MolarFlow>
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              <Descricao></Descricao>
              <Nome>Etano</Nome>
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              <Descricao></Descricao>
              <Nome>nButano</Nome>
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          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 3</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>6</ID>
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            <Compound>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
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              <VolumetricFlow>0</VolumetricFlow>
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              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
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              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Aqueous</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>nButano</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Solid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.EnergyStream</Type>
      <Energia>475.886828407626</Energia>
      <ComponentDescription>EN-b2cf52bc-24ce-441d-a0d2-ef506122d6fb</ComponentDescription>
      <ComponentName>e1</ComponentName>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>Correntedeenergia</Descricao>
      <Nome>EN-b2cf52bc-24ce-441d-a0d2-ef506122d6fb</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
    </SimulationObject>
  </SimulationObjects>
  <GraphicObjects>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.HeaterGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Aquecedor</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>Heater</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>HEAT-000</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5335</X>
      <Y>3661</Y>
      <Name>AQ-92096e77-60c8-488f-b8ef-1d580c6715c7</Name>
      <Height>25</Height>
      <Width>25</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="MAT-48f6141f-8248-406f-b972-58f9e9672b9d" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
        <Connector IsAttached="True" ConnType="ConEn" AttachedFromObjID="EN-b2cf52bc-24ce-441d-a0d2-ef506122d6fb" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="MAT-1423c3a0-7f96-4c79-ae7c-1fecc86cf797" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>input</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5252</X>
      <Y>3660</Y>
      <Name>MAT-48f6141f-8248-406f-b972-58f9e9672b9d</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="AQ-92096e77-60c8-488f-b8ef-1d580c6715c7" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>output</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5436</X>
      <Y>3657</Y>
      <Name>MAT-1423c3a0-7f96-4c79-ae7c-1fecc86cf797</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="AQ-92096e77-60c8-488f-b8ef-1d580c6715c7" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.EnergyStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>LightYellow</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Correntedeenergia</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>EnergyStream</TipoObjeto>
      <IsEnergyStream>true</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>e1</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5316</X>
      <Y>3706</Y>
      <Name>EN-b2cf52bc-24ce-441d-a0d2-ef506122d6fb</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="AQ-92096e77-60c8-488f-b8ef-1d580c6715c7" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
  </GraphicObjects>
  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-a26ec457-f2ab-4ba6-81a0-bb4d69a3d30b</ID>
      <Type>DWSIM.DWSIM.SimulationObjects.PropertyPackages.PengRobinsonPropertyPackage</Type>
      <ComponentName>Peng-Robinson (PR)</ComponentName>
      <ComponentDescription>Property Package that uses the Peng-Robinson EOS. Recommended for use with hydrocarbons and non-condensables.
The properties are calculated directly from the EOS and/or experimental data, except:
Liquid Density: Rackett Method
Liquid Thermal Conductivity: Latini et al Method
Vapor Thermal Conductivity: Ely-Hanley Method
Liquid Surface Tension: Brock-Bird Method</ComponentDescription>
      <Tag>PP_1</Tag>
      <IOQUick>true</IOQUick>
      <TPSeverity>0</TPSeverity>
      <TPCompIDs>Etano,nButano</TPCompIDs>
      <Parameters>
        <Parameter ID="PP_PHFILT" Value="0.001" />
        <Parameter ID="PP_PSFILT" Value="0.001" />
        <Parameter ID="PP_PHFELT" Value="0.001" />
        <Parameter ID="PP_PSFELT" Value="0.001" />
        <Parameter ID="PP_PHFMEI" Value="50" />
        <Parameter ID="PP_PSFMEI" Value="50" />
        <Parameter ID="PP_PHFMII" Value="100" />
        <Parameter ID="PP_PSFMII" Value="100" />
        <Parameter ID="PP_PTFMEI" Value="100" />
        <Parameter ID="PP_PTFMII" Value="100" />
        <Parameter ID="PP_PTFILT" Value="0.001" />
        <Parameter ID="PP_PTFELT" Value="0.001" />
        <Parameter ID="PP_FLASHALGORITHM" Value="2" />
        <Parameter ID="PP_IDEAL_MIXRULE_LIQDENS" Value="0" />
        <Parameter ID="PP_USEEXPLIQDENS" Value="0" />
        <Parameter ID="PP_USE_EOS_LIQDENS" Value="0" />
        <Parameter ID="PP_USE_EOS_VOLUME_SHIFT" Value="0" />
      </Parameters>
      <InteractionParameters>
        <InteractionParameter Compound1="Etano" Compound2="nButano" Value="0.0089" />
      </InteractionParameters>
    </PropertyPackage>
  </PropertyPackages>
  <Compounds>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Etano</Name>
      <CAS_Number>74-84-0</CAS_Number>
      <Formula>C2H6</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>30.07</Molar_Weight>
      <Critical_Temperature>305.32</Critical_Temperature>
      <Critical_Pressure>4872000</Critical_Pressure>
      <Critical_Volume>0.1455</Critical_Volume>
      <Critical_Compressibility>0.279</Critical_Compressibility>
      <Acentric_Factor>0.09949</Acentric_Factor>
      <Z_Rackett>0.281</Z_Rackett>
      <PR_Volume_Translation_Coefficient>-0.1134</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0.0605</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.1064</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>6.05</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>68</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>3.1775</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-2787.5</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-1061.54</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>51.857</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-2598.7</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-5.1283</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>1.49E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>90.35</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>305.32</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>33.3</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-0.0111</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>0.000357</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-3.76E-07</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.19E-10</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-70.046</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>276.38</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-0.6087</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-3.11E-18</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>7</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>184.55</Normal_Boiling_Point>
      <ID>2</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>21091000</HVap_A>
      <HVap_B>0.6046</HVap_B>
      <HVap_C>-0.55492</HVap_C>
      <HVap_D>0.32799</HVap_D>
      <HVap_TMIN>90</HVap_TMIN>
      <HVap_TMAX>305</HVap_TMAX>
      <UNIQUAC_R>1.8022</UNIQUAC_R>
      <UNIQUAC_Q>1.696</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName>ETHANE</COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="CH3" Value="2" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH3" Value="2" />
      </MODFACGroups>
      <Elements>
        <Item Name="C" Value="2" />
        <Item Name="H" Value="6" />
      </Elements>
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>nButano</Name>
      <CAS_Number>106-97-8</CAS_Number>
      <Formula>C4H10</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>58.123</Molar_Weight>
      <Critical_Temperature>425.12</Critical_Temperature>
      <Critical_Pressure>3800000</Critical_Pressure>
      <Critical_Volume>0.255</Critical_Volume>
      <Critical_Compressibility>0.274</Critical_Compressibility>
      <Acentric_Factor>0.200164</Acentric_Factor>
      <Z_Rackett>0.275</Z_Rackett>
      <PR_Volume_Translation_Coefficient>-0.0675</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0.0975</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.1953</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>6.73</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>101.4</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>4.29792</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-2164.2</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-287.32</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>66.343</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-4363.2</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-7.046</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>9.45E-06</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>134</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>425</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>24.1</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>0.209</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>0.000217</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-3.37E-07</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.16E-10</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-72.471</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>534.82</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-0.57469</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-4.66E-27</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>10</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>272.65</Normal_Boiling_Point>
      <ID>4</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>36238000</HVap_A>
      <HVap_B>0.8337</HVap_B>
      <HVap_C>-0.82274</HVap_C>
      <HVap_D>0.39613</HVap_D>
      <HVap_TMIN>135</HVap_TMIN>
      <HVap_TMAX>425</HVap_TMAX>
      <UNIQUAC_R>3.151</UNIQUAC_R>
      <UNIQUAC_Q>2.776</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName>N-BUTANE</COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
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        <Item Name="CH3" Value="2" />
      </UNIFACGroups>
      <MODFACGroups>
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        <Item Name="CH3" Value="2" />
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      <Elements>
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        <Item Name="H" Value="10" />
      </Elements>
    </Compound>
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  <ReactionSets>
    <ReactionSet>
      <ID>DefaultSet</ID>
      <Name>Default Set</Name>
      <Description>Default Reaction Set</Description>
      <Reactions />
    </ReactionSet>
  </ReactionSets>
  <Reactions />
  <OptimizationCases />
  <SensitivityAnalysis />
  <PetroleumAssays />
  <WatchItems />
  <Spreadsheet>
    <Data1></Data1>
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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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