<?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>2014-12-11T16:17:50.5815233-08:00</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></FilePath>
    <BackupFileName>34329754.dwbcs</BackupFileName>
    <CalculatorActivated>true</CalculatorActivated>
    <PropertyPackageFlashAlgorithm>DWSIMDefault</PropertyPackageFlashAlgorithm>
    <PropertyPackageIOFlashQuickMode>true</PropertyPackageIOFlashQuickMode>
    <ThreePhaseFlashStabTestSeverity>0</ThreePhaseFlashStabTestSeverity>
    <FlashValidationDGETolerancePct>0.01</FlashValidationDGETolerancePct>
    <Password></Password>
    <UsePassword>false</UsePassword>
    <ThreePhaseFlashStabTestCompIds>Propane,Propylene,Hydrogen</ThreePhaseFlashStabTestCompIds>
  </Settings>
  <SimulationObjects>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Propane</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-76cc9381-140c-4377-84c6-9c0a586651d2</ComponentDescription>
      <ComponentName>feed</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-76cc9381-140c-4377-84c6-9c0a586651d2</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>1</FracaoMolar>
              <FracaoMassica>1</FracaoMassica>
              <MolarFlow>100</MolarFlow>
              <MassFlow>4.4097</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>5.89489188924355</density>
            <enthalpy>1766.55091511138</enthalpy>
            <entropy>2.79745308196833</entropy>
            <molarflow>100</molarflow>
            <massflow>4.4097</massflow>
            <heatCapacityCp>3.75175058189862</heatCapacityCp>
            <heatCapacityCv>3.55728563149502</heatCapacityCv>
            <molecularWeight>44.097</molecularWeight>
            <pressure>1000000</pressure>
            <temperature>900</temperature>
            <thermalConductivity>0.122843836264079</thermalConductivity>
            <volumetric_flow>0.7480544313368</volumetric_flow>
            <molar_enthalpy>77899.5957036666</molar_enthalpy>
            <molar_entropy>123.359288555558</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</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>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</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>1</FracaoMolar>
              <FracaoMassica>1</FracaoMassica>
              <MolarFlow>100</MolarFlow>
              <MassFlow>4.4097</MassFlow>
              <FugacityCoeff>0.999638174950861</FugacityCoeff>
              <ActivityCoeff>0.000297716245209561</ActivityCoeff>
              <PartialVolume>0.007480544382652</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.7480544313368</VolumetricFlow>
              <VolumetricFraction>1</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</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>0.999798537513444</FugacityCoeff>
              <ActivityCoeff>2.339483700043E-06</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</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>1.00623608648153</FugacityCoeff>
              <ActivityCoeff>2.51910658405116E-115</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.999725271077967</compressibilityFactor>
            <density>5.89489188924355</density>
            <enthalpy>1766.55091511138</enthalpy>
            <entropy>2.79745308196833</entropy>
            <molarflow>100</molarflow>
            <massflow>4.4097</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.75175058189862</heatCapacityCp>
            <heatCapacityCv>3.55728563149502</heatCapacityCv>
            <molecularWeight>44.097</molecularWeight>
            <thermalConductivity>0.122843836264079</thermalConductivity>
            <viscosity>2.27132167826396E-05</viscosity>
            <kinematic_viscosity>3.85303364495701E-06</kinematic_viscosity>
            <volumetric_flow>0.7480544313368</volumetric_flow>
            <molar_enthalpy>77899.5957036666</molar_enthalpy>
            <molar_entropy>123.359288555558</molar_entropy>
          </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</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>Propane</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>Propylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>
              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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.UnitOps.Mixer</Type>
      <PressureCalculation>Average</PressureCalculation>
      <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>PH Flash [NL]: Invalid result: Temperature did not converge.</ErrorMessage>
      <ComponentDescription>Misturador</ComponentDescription>
      <ComponentName>MIST-ce224e6c-69f8-4bf1-9590-78d35d38f6fc</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>Misturador</Descricao>
      <Nome>MIST-ce224e6c-69f8-4bf1-9590-78d35d38f6fc</Nome>
      <ShowQuickTable>false</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Propane</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-31026018-ac1f-47fc-a548-4022eb525d23</ComponentDescription>
      <ComponentName>rec2</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-31026018-ac1f-47fc-a548-4022eb525d23</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.98821232436155</FracaoMolar>
              <FracaoMassica>0.988745504720593</FracaoMassica>
              <MolarFlow>67.5311325425931</MolarFlow>
              <MassFlow>2.97792035173073</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.01178767563845</FracaoMolar>
              <FracaoMassica>0.0112544952794072</FracaoMassica>
              <MolarFlow>0.805660836362132</MolarFlow>
              <MassFlow>0.0339019662958676</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>5.89170268768738</density>
            <enthalpy>1764.13828728828</enthalpy>
            <entropy>2.80545031235543</entropy>
            <molarflow>68.3367933789552</molarflow>
            <massflow>3.00572902346834</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.74628141380239</heatCapacityCp>
            <heatCapacityCv>3.5517189213727</heatCapacityCv>
            <molecularWeight>44.0732169173467</molecularWeight>
            <pressure>999999.999973807</pressure>
            <temperature>899.999999999999</temperature>
            <thermalConductivity>0.122676177295234</thermalConductivity>
            <volumetric_flow>0.511197268036076</volumetric_flow>
            <molar_enthalpy>77751.2323858512</molar_enthalpy>
            <molar_entropy>123.645220167279</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</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</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</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>0.98821232436155</FracaoMolar>
              <FracaoMassica>0.988745504720593</FracaoMassica>
              <MolarFlow>67.5311325425931</MolarFlow>
              <MassFlow>2.97792035173073</MassFlow>
              <FugacityCoeff>0.999638197160589</FugacityCoeff>
              <ActivityCoeff>0.000297716251808564</ActivityCoeff>
              <PartialVolume>0.00748054438265198</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.505169640335171</VolumetricFlow>
              <VolumetricFraction>0.988208802985075</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.01178767563845</FracaoMolar>
              <FracaoMassica>0.0112544952794072</FracaoMassica>
              <MolarFlow>0.805660836362132</MolarFlow>
              <MassFlow>0.0339019662958676</MassFlow>
              <FugacityCoeff>0.999794791449766</FugacityCoeff>
              <ActivityCoeff>2.33947493429978E-06</ActivityCoeff>
              <PartialVolume>0.00748159443229921</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.00602762770090488</VolumetricFlow>
              <VolumetricFraction>0.0117911970149252</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</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>1.00622936599503</FugacityCoeff>
              <ActivityCoeff>2.51908975922142E-115</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.999726946890071</compressibilityFactor>
            <density>5.89170268768738</density>
            <enthalpy>1764.13790106729</enthalpy>
            <entropy>2.80545031235543</entropy>
            <molarflow>68.3367933789552</molarflow>
            <massflow>3.01182231802659</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>44.0732207219346</massfraction>
            <heatCapacityCp>3.74628141380239</heatCapacityCp>
            <heatCapacityCv>3.5517189213727</heatCapacityCv>
            <molecularWeight>44.0732169173467</molecularWeight>
            <thermalConductivity>0.122676177295234</thermalConductivity>
            <viscosity>2.2719359790837E-05</viscosity>
            <kinematic_viscosity>3.85616196117914E-06</kinematic_viscosity>
            <volumetric_flow>0.511197268036076</volumetric_flow>
            <molar_enthalpy>77751.2323858512</molar_enthalpy>
            <molar_entropy>123.645220167279</molar_entropy>
          </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</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>Propane</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>Propylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>
              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-76c248c3-f5ea-4012-b3df-e6dbfe3a3c53</ComponentDescription>
      <ComponentName>mix</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-76c248c3-f5ea-4012-b3df-e6dbfe3a3c53</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.995213994396647</FracaoMolar>
              <FracaoMassica>0.995431939049281</FracaoMassica>
              <MolarFlow>167.531132542593</MolarFlow>
              <MassFlow>7.38762035173073</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00478600560335286</FracaoMolar>
              <FracaoMassica>0.0045680609507191</FracaoMassica>
              <MolarFlow>0.805660836362131</MolarFlow>
              <MassFlow>0.0339019662958676</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>5.89359719140355</density>
            <enthalpy>1765.57166240278</enthalpy>
            <entropy>2.80155583461421</entropy>
            <molarflow>168.336793378955</molarflow>
            <massflow>7.42152231802659</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.7495310633028</heatCapacityCp>
            <heatCapacityCv>3.55502653228325</heatCapacityCv>
            <molecularWeight>44.0873451908964</molecularWeight>
            <pressure>999999.999973807</pressure>
            <temperature>899.999999999999</temperature>
            <thermalConductivity>0.122775774635471</thermalConductivity>
            <volumetric_flow>1.25925170604664</volumetric_flow>
            <molar_enthalpy>77839.3673396162</molar_enthalpy>
            <molar_entropy>123.513159152206</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</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>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</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>0.995213994396647</FracaoMolar>
              <FracaoMassica>0.995431939049281</FracaoMassica>
              <MolarFlow>167.531132542593</MolarFlow>
              <MassFlow>7.38762035173072</MassFlow>
              <FugacityCoeff>0.999638178610951</FugacityCoeff>
              <ActivityCoeff>0.000297716246291828</ActivityCoeff>
              <PartialVolume>0.00748054438265199</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>1.25322406560159</VolumetricFlow>
              <VolumetricFraction>0.995213315641264</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00478600560335286</FracaoMolar>
              <FracaoMassica>0.0045680609507191</FracaoMassica>
              <MolarFlow>0.805660836362131</MolarFlow>
              <MassFlow>0.0339019662958676</MassFlow>
              <FugacityCoeff>0.99979701143815</FugacityCoeff>
              <ActivityCoeff>2.33948012903412E-06</ActivityCoeff>
              <PartialVolume>0.00748161038242045</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.00602764044504559</VolumetricFlow>
              <VolumetricFraction>0.00478668435873642</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</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>1.00623335288849</FugacityCoeff>
              <ActivityCoeff>2.51909974045112E-115</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.999725956671998</compressibilityFactor>
            <density>5.89359719140355</density>
            <enthalpy>1765.57166240278</enthalpy>
            <entropy>2.80155583461421</entropy>
            <molarflow>168.336793378955</molarflow>
            <massflow>7.42152231802659</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.7495310633028</heatCapacityCp>
            <heatCapacityCv>3.55502653228325</heatCapacityCv>
            <molecularWeight>44.0873451908964</molecularWeight>
            <thermalConductivity>0.122775774635471</thermalConductivity>
            <viscosity>2.27157105877201E-05</viscosity>
            <kinematic_viscosity>3.85430321245121E-06</kinematic_viscosity>
            <volumetric_flow>1.25925170604664</volumetric_flow>
            <molar_enthalpy>77839.3673396162</molar_enthalpy>
            <molar_entropy>123.513159152206</molar_entropy>
          </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</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>Propane</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>Propylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
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          <Compounds>
            <Compound>
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              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>
              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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.Reactors.Reactor_Conversion</Type>
      <ReactorOperationMode>Isothermic</ReactorOperationMode>
      <ReactionSetID>DefaultSet</ReactionSetID>
      <ReactionSetName></ReactionSetName>
      <DeltaT>0</DeltaT>
      <DeltaQ>2094.31433746822</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>Index was outside the bounds of the array.</ErrorMessage>
      <ComponentDescription>ReatorConversao</ComponentDescription>
      <ComponentName>RC-82ae444c-0090-4bd5-9bf2-c57618748df1</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>ReatorConversao</Descricao>
      <Nome>RC-82ae444c-0090-4bd5-9bf2-c57618748df1</Nome>
      <ShowQuickTable>false</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
      <ReactionSequence>
        <Item Index="0">bdddf5ee-6f42-4899-9bde-0f2cdf0a8cee</Item>
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      <Reactions>
        <Reaction ID="bdddf5ee-6f42-4899-9bde-0f2cdf0a8cee" />
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      <ReactionConversions>
        <Reaction ID="bdddf5ee-6f42-4899-9bde-0f2cdf0a8cee">0.096</Reaction>
      </ReactionConversions>
      <CompoundConversions />
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-3b006523-972f-42dc-8509-4090a8c17786</ComponentDescription>
      <ComponentName>out1</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-3b006523-972f-42dc-8509-4090a8c17786</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</PropertyPackage>
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            <Compound>
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              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.821214199970602</FracaoMolar>
              <FracaoMassica>0.899873242031172</FracaoMassica>
              <MolarFlow>151.448609863013</MolarFlow>
              <MassFlow>6.67842934912929</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0915772124219005</FracaoMolar>
              <FracaoMassica>0.0957581832090119</FracaoMassica>
              <MolarFlow>16.8887015311269</MolarFlow>
              <MassFlow>0.710671493819361</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0872085876074976</FracaoMolar>
              <FracaoMassica>0.00436857475981642</FracaoMassica>
              <MolarFlow>16.0830382155412</MolarFlow>
              <MassFlow>0.0324214750779452</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>5.37674171517222</density>
            <enthalpy>1777.07714770394</enthalpy>
            <entropy>3.73156563376816</entropy>
            <molarflow>184.420349609681</molarflow>
            <massflow>7.42152231802659</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.75307301661837</heatCapacityCp>
            <heatCapacityCv>3.5408781524122</heatCapacityCv>
            <molecularWeight>40.2424262492397</molecularWeight>
            <pressure>999999.999973807</pressure>
            <temperature>899.999999999999</temperature>
            <thermalConductivity>0.147146532540614</thermalConductivity>
            <volumetric_flow>1.38030106543604</volumetric_flow>
            <molar_enthalpy>71513.8960556851</molar_enthalpy>
            <molar_entropy>150.167254811113</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</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>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</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>0.821214199970602</FracaoMolar>
              <FracaoMassica>0.899873242031172</FracaoMassica>
              <MolarFlow>151.448609863013</MolarFlow>
              <MassFlow>6.67842934912929</MassFlow>
              <FugacityCoeff>0.99967743262744</FugacityCoeff>
              <ActivityCoeff>0.000297727937080246</ActivityCoeff>
              <PartialVolume>0.00748083148483402</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>1.13296155948837</VolumetricFlow>
              <VolumetricFraction>0.820807567174096</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0915772124219005</FracaoMolar>
              <FracaoMassica>0.0957581832090119</FracaoMassica>
              <MolarFlow>16.8887015311269</MolarFlow>
              <MassFlow>0.710671493819362</MassFlow>
              <FugacityCoeff>0.999758952738376</FugacityCoeff>
              <ActivityCoeff>2.33939107338498E-06</ActivityCoeff>
              <PartialVolume>0.00748133391365257</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.126350018922767</VolumetricFlow>
              <VolumetricFraction>0.0915380144858855</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0872085876074976</FracaoMolar>
              <FracaoMassica>0.00436857475981642</FracaoMassica>
              <MolarFlow>16.0830382155412</MolarFlow>
              <MassFlow>0.0324214750779452</MassFlow>
              <FugacityCoeff>1.00545299484804</FugacityCoeff>
              <ActivityCoeff>2.51714611833007E-115</ActivityCoeff>
              <PartialVolume>0.00752280024130413</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.120989487024903</VolumetricFlow>
              <VolumetricFraction>0.087654418340018</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>1.00025896520881</compressibilityFactor>
            <density>5.37674171517222</density>
            <enthalpy>1777.07714770394</enthalpy>
            <entropy>3.73156563376816</entropy>
            <molarflow>184.420349609681</molarflow>
            <massflow>7.42152231802659</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.75307301661837</heatCapacityCp>
            <heatCapacityCv>3.5408781524122</heatCapacityCv>
            <molecularWeight>40.2424262492397</molecularWeight>
            <thermalConductivity>0.147146532540614</thermalConductivity>
            <viscosity>2.24389071051147E-05</viscosity>
            <kinematic_viscosity>4.17332806628892E-06</kinematic_viscosity>
            <volumetric_flow>1.38030106543604</volumetric_flow>
            <molar_enthalpy>71513.8960556851</molar_enthalpy>
            <molar_entropy>150.167254811113</molar_entropy>
          </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</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>Propane</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>Propylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>
              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-14a6beb6-78c1-4090-9039-d137ec7bbf37</ComponentDescription>
      <ComponentName>liq</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-14a6beb6-78c1-4090-9039-d137ec7bbf37</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>NaN</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>NaN</molarflow>
            <massflow>0</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>0</molecularWeight>
            <pressure>999999.999973807</pressure>
            <temperature>899.999999999999</temperature>
            <thermalConductivity>0</thermalConductivity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</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>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</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</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</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>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</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>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>1</compressibilityFactor>
            <density>0</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>NaN</molarflow>
            <massflow>NaN</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>NaN</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>0</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>NaN</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>0</molar_enthalpy>
            <molar_entropy>0</molar_entropy>
          </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</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>Propane</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>Propylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>
              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>2094.31433746822</Energia>
      <ComponentDescription>EN-3dfea978-09b4-4e54-9339-d9b9549ff30e</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-3dfea978-09b4-4e54-9339-d9b9549ff30e</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.UnitOps.ComponentSeparator</Type>
      <SpecifiedStreamIndex>0</SpecifiedStreamIndex>
      <EnergyImb>0.121701552205195</EnergyImb>
      <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>ComponentSeparator</ComponentDescription>
      <ComponentName>CS-5f2cf80a-c0a3-415a-84ff-4e70fa8127a7</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>ComponentSeparator</Descricao>
      <Nome>CS-5f2cf80a-c0a3-415a-84ff-4e70fa8127a7</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
      <SeparationSpecs>
        <SeparationSpec ID="Propane" CompID="Propane" SepSpec="PercentInletMolarFlow" SpecUnit="%" SpecValue="44.5" />
        <SeparationSpec ID="Propylene" CompID="Propylene" SepSpec="PercentInletMolarFlow" SpecUnit="%" SpecValue="4.76" />
        <SeparationSpec ID="Hydrogen" CompID="Hydrogen" SepSpec="PercentInletMolarFlow" SpecUnit="%" SpecValue="0" />
      </SeparationSpecs>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-659f4a77-7312-4177-a714-40c65f976f62</ComponentDescription>
      <ComponentName>rec1</ComponentName>
      <code>0</code>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
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              <Nome>Hydrogen</Nome>
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            <molar_entropy>NaN</molar_entropy>
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          <Nome>Liquid 1</Nome>
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              <Nome>Hydrogen</Nome>
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              <Nome>Propylene</Nome>
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              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 3</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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              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
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              <VolumetricFlow>0</VolumetricFlow>
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              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
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              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</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>
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        </Phase>
        <Phase>
          <ID>7</ID>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
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              <FracaoMassica>0</FracaoMassica>
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              <ActivityCoeff>0</ActivityCoeff>
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              <VolumetricFlow>0</VolumetricFlow>
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              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
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              <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>Propylene</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>Hydrogen</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.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <CompositionBasis>Molar_Flows</CompositionBasis>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-842ef149-234e-4097-a74c-201a61e0ca01</ComponentDescription>
      <ComponentName>out</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-842ef149-234e-4097-a74c-201a61e0ca01</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.723220315658263</FracaoMolar>
              <FracaoMassica>0.839379935046879</FracaoMassica>
              <MolarFlow>84.0539784739722</MolarFlow>
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              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
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              <FracaoMolar>0.138397418729058</FracaoMolar>
              <FracaoMassica>0.153277901741383</FracaoMassica>
              <MolarFlow>16.0847993382453</MolarFlow>
              <MassFlow>0.67684353071356</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
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              <FracaoMolar>0.138382265612679</FracaoMolar>
              <FracaoMassica>0.00734216321173805</FracaoMassica>
              <MolarFlow>16.0830382155412</MolarFlow>
              <MassFlow>0.0324214750779452</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>5.07499646010533</density>
            <enthalpy>1785.85677214368</enthalpy>
            <entropy>3.99889807721429</entropy>
            <molarflow>116.221816027759</molarflow>
            <massflow>4.41579329455826</massflow>
            <heatCapacityCp>3.75775055633696</heatCapacityCp>
            <heatCapacityCv>3.53352021379557</heatCapacityCv>
            <molecularWeight>37.9945301620789</molecularWeight>
            <pressure>999999.999973807</pressure>
            <temperature>899.999999999999</temperature>
            <thermalConductivity>0.1615056311323</thermalConductivity>
            <volumetric_flow>0.870107660029109</volumetric_flow>
            <molar_enthalpy>67852.788994366</molar_enthalpy>
            <molar_entropy>151.936253609797</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</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>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</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>0.723220315658263</FracaoMolar>
              <FracaoMassica>0.839379935046879</FracaoMassica>
              <MolarFlow>84.0539784739722</MolarFlow>
              <MassFlow>3.70652828876675</MassFlow>
              <FugacityCoeff>0.999736170735872</FugacityCoeff>
              <ActivityCoeff>0.000297745430698968</ActivityCoeff>
              <PartialVolume>0.00748126213810706</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.628829838910535</VolumetricFlow>
              <VolumetricFraction>0.722703485784159</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.138397418729058</FracaoMolar>
              <FracaoMassica>0.153277901741383</FracaoMassica>
              <MolarFlow>16.0847993382453</MolarFlow>
              <MassFlow>0.67684353071356</MassFlow>
              <FugacityCoeff>0.999773616551898</FugacityCoeff>
              <ActivityCoeff>2.33942538605041E-06</ActivityCoeff>
              <PartialVolume>0.0074814429061476</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.120337506412481</VolumetricFlow>
              <VolumetricFraction>0.13830185842572</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Propylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.138382265612679</FracaoMolar>
              <FracaoMassica>0.00734216321173805</FracaoMassica>
              <MolarFlow>16.0830382155412</MolarFlow>
              <MassFlow>0.0324214750779452</MassFlow>
              <FugacityCoeff>1.00503360735284</FugacityCoeff>
              <ActivityCoeff>2.51609618401089E-115</ActivityCoeff>
              <PartialVolume>0.00751974313473624</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.120940314706093</VolumetricFlow>
              <VolumetricFraction>0.138994655790121</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>1.0005361973546</compressibilityFactor>
            <density>5.07499646010533</density>
            <enthalpy>1785.85677214368</enthalpy>
            <entropy>3.99889807721429</entropy>
            <molarflow>116.221816027759</molarflow>
            <massflow>4.41579329455826</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.75775055633696</heatCapacityCp>
            <heatCapacityCv>3.53352021379557</heatCapacityCv>
            <molecularWeight>37.9945301620789</molecularWeight>
            <thermalConductivity>0.1615056311323</thermalConductivity>
            <viscosity>2.22746779909336E-05</viscosity>
            <kinematic_viscosity>4.38910217298383E-06</kinematic_viscosity>
            <volumetric_flow>0.870107660029109</volumetric_flow>
            <molar_enthalpy>67852.788994366</molar_enthalpy>
            <molar_entropy>151.936253609797</molar_entropy>
          </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</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>Propane</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>Propylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>
              <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>Propane</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>Propylene</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>Hydrogen</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>Propane</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>Propylene</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>Hydrogen</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>0.121701552205195</Energia>
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      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>Correntedeenergia</Descricao>
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      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
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      <FlashType>FlashTP</FlashType>
      <AccelerationMethod>Wegstein</AccelerationMethod>
      <ConvergenceParameters>
        <Temperatura>0.1</Temperatura>
        <Pressao>0.1</Pressao>
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        <FracaoVapor>0.01</FracaoVapor>
        <Entalpia>1</Entalpia>
        <Entropia>0.01</Entropia>
        <Composicao>0.001</Composicao>
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      <ConvergenceHistory>
        <Temperatura>899.999999999999</Temperatura>
        <Pressao>999999.999973807</Pressao>
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        <Entropia>0</Entropia>
        <Temperatura0>899.999999999998</Temperatura0>
        <Pressao0>999999.999947613</Pressao0>
        <VazaoMassica0>3.01182231802659</VazaoMassica0>
        <Entalpia0>0</Entalpia0>
        <Entropia0>0</Entropia0>
        <TemperaturaE>1.59161572810262E-12</TemperaturaE>
        <PressaoE>2.61934474110603E-05</PressaoE>
        <VazaoMassicaE>-0.00609329455825813</VazaoMassicaE>
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        <EntropiaE>0</EntropiaE>
        <TemperaturaE0>3.63797880709171E-12</TemperaturaE0>
        <PressaoE0>5.23868948221207E-05</PressaoE0>
        <VazaoMassicaE0>-0.0151468528114678</VazaoMassicaE0>
        <EntalpiaE0>0</EntalpiaE0>
        <EntropiaE0>0</EntropiaE0>
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      <MaximumIterations>10</MaximumIterations>
      <ScriptExt_FontName>Courier New</ScriptExt_FontName>
      <ScriptExt_FontSize>10</ScriptExt_FontSize>
      <ScriptExt_ScriptTextB></ScriptExt_ScriptTextB>
      <ScriptExt_ScriptTextA></ScriptExt_ScriptTextA>
      <ScriptExt_Language>IronPython</ScriptExt_Language>
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      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>Reciclo</Descricao>
      <Nome>REC-f84710eb-dbfc-4b2a-b6da-93f26f855c03</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
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      <PropertyPackage></PropertyPackage>
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  </SimulationObjects>
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      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
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      <EnergyConnector AttachedFromObjID="CS-5f2cf80a-c0a3-415a-84ff-4e70fa8127a7" AttachedFromConnIndex="-1" AttachedFromEnergyConn="False">
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      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>WhiteSmoke</FillColor>
      <LineWidth>2</LineWidth>
      <Width>20</Width>
      <Height>20</Height>
      <Rotation>0</Rotation>
      <X>5355</X>
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      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
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      <Shape>0</Shape>
      <FlippedH>true</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
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      <EnergyConnector>
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      <SpecialConnectors />
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    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>WhiteSmoke</FillColor>
      <LineWidth>2</LineWidth>
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      <Rotation>0</Rotation>
      <X>5505</X>
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      <LineColor>SteelBlue</LineColor>
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      <EnergyConnector>
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      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
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      <EnergyConnector>
        <Connector IsAttached="False" />
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      <SpecialConnectors />
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    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.RecycleGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
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      <SplitPoint>false</SplitPoint>
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      <Shape>0</Shape>
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      <FlippedV>false</FlippedV>
      <TipoObjeto>OT_Reciclo</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>REC-000</Tag>
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      <IsConnector>false</IsConnector>
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      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="MAT-31026018-ac1f-47fc-a548-4022eb525d23" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
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      <EnergyConnector>
        <Connector IsAttached="False" />
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  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-b6e2dacf-c047-4caa-b6f1-c6a6fe105e86</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>Propane,Propylene,Hydrogen</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="Hydrogen" Compound2="Propylene" Value="-0.1037" />
        <InteractionParameter Compound1="Hydrogen" Compound2="Propane" Value="-0.1311" />
        <InteractionParameter Compound1="Propylene" Compound2="Propane" Value="0.0096" />
      </InteractionParameters>
    </PropertyPackage>
  </PropertyPackages>
  <Compounds>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Propane</Name>
      <CAS_Number>74-98-6</CAS_Number>
      <Formula>CH3CH2CH3</Formula>
      <SMILES>CCC</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>44.097</Molar_Weight>
      <Critical_Temperature>369.83</Critical_Temperature>
      <Critical_Pressure>4248000</Critical_Pressure>
      <Critical_Volume>0.2</Critical_Volume>
      <Critical_Compressibility>0.276</Critical_Compressibility>
      <Acentric_Factor>0.152</Acentric_Factor>
      <Z_Rackett>0.2763</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.1538</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.0031267807552</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>84</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>6.1274009569812</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-2373.85763203846</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-553.098850261923</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>48.155</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-3122.7</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-4.3265</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>8.2466E-06</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>85.47</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>371.25</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>37840.4</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-445.5789</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>11.83871</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>0.000653764</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>-2.200137E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-20.236</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>689.15</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>1.7071</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-1.0696E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>1.3186</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.27005</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>369.86</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.27852</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>85.47</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>369.85</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>87486</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-13371</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>156.92</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-0.5459</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.00068504</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>85.47</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>360</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0.02937</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-16.323</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-1.3313</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.0012596</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-1.1206E-05</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>85.47</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>350</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>-1.139</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.10904</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>-9898.6</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-7669600</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>231.11</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1000</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>4.7422E-08</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.90416</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>-4.7484</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>478.57</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>85.47</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>18.861</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.020332</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>23.15</Solid_Density_Tmin>
      <Solid_Density_Tmax>85.48</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.0093557</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>17.245</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-3.1909</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.00024043</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-1.1944E-05</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>85.44</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>369.98</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>-9928.1</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>957.89</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>-0.77533</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-0.03376</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.00014632</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>30</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>84</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>231.02</Normal_Boiling_Point>
      <ID>3</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>30459000</HVap_A>
      <HVap_B>1.2001</HVap_B>
      <HVap_C>-2.1107</HVap_C>
      <HVap_D>1.9732</HVap_D>
      <HVap_TMIN>85.44</HVap_TMIN>
      <HVap_TMAX>369.85</HVap_TMAX>
      <UNIQUAC_R>2.4766</UNIQUAC_R>
      <UNIQUAC_Q>2.236</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation>101</VaporPressureEquation>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <SolidDensityEquation>2</SolidDensityEquation>
      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
      <SurfaceTensionEquation>16</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>ChemSep</OriginalDB>
      <CurrentDB>ChemSep</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName></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>85.47</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>3.524</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="CH2" Value="1" />
        <Item Name="CH3" Value="2" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH2" Value="1" />
        <Item Name="CH3" Value="2" />
      </MODFACGroups>
      <Elements />
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Propylene</Name>
      <CAS_Number>115-07-1</CAS_Number>
      <Formula>CH2CHCH3</Formula>
      <SMILES>C=CC</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>42.0797</Molar_Weight>
      <Critical_Temperature>364.85</Critical_Temperature>
      <Critical_Pressure>4600000</Critical_Pressure>
      <Critical_Volume>0.185</Critical_Volume>
      <Critical_Compressibility>0.281</Critical_Compressibility>
      <Acentric_Factor>0.137588</Acentric_Factor>
      <Z_Rackett>0.2785</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.1477</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.0031413981304</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>68.956</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>6.3451022702158</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>480.754378001744</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>1488.60376856299</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>1.22E-30</Dipole_Moment>
      <Vapor_Pressure_Constant_A>90.171</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-4383.8</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-11.125</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>2.1182E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>87.89</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>365.57</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>38965.36</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-516.3838</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>11.75322</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>0.000509119</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>-1.771348E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-82.854</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>1932.2</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>12.786</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-6.8648E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0.98129</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.22226</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>365.58</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.24039</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>87.89</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>365.57</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>79790</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>300.8</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>5.1342</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0.0095615</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>1.2777E-05</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>87.85</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>340</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.044587</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>22.061</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-1.744</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0.0015214</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-7.8162E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>87.89</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>340.49</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>4.5373E-05</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>1.2</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>415.83</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>2757.2</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>225.45</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1000</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>7.3873E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.54213</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>262.33</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>-108.51</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>87.89</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>20.846</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.020946</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>73.15</Solid_Density_Tmin>
      <Solid_Density_Tmax>88.1</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.012171</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>10.886</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-2.9978</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>-0.00044205</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-9.7257E-06</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>87.89</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>364.85</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>-1062</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-87.684</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>46.783</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-0.8344</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.0046648</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>14</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>87.89</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>225.45</Normal_Boiling_Point>
      <ID>202</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>27525000</HVap_A>
      <HVap_B>0.61217</HVap_B>
      <HVap_C>-0.41646</HVap_C>
      <HVap_D>0.083772</HVap_D>
      <HVap_TMIN>87.89</HVap_TMIN>
      <HVap_TMAX>365</HVap_TMAX>
      <UNIQUAC_R>2.25</UNIQUAC_R>
      <UNIQUAC_Q>2.02</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation>101</VaporPressureEquation>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <SolidDensityEquation>2</SolidDensityEquation>
      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
      <SurfaceTensionEquation>16</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>ChemSep</OriginalDB>
      <CurrentDB>ChemSep</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName></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>87.9</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>2.936</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="CH2=CH" Value="1" />
        <Item Name="CH3" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH2=CH" Value="1" />
        <Item Name="CH3" Value="1" />
      </MODFACGroups>
      <Elements />
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Hydrogen</Name>
      <CAS_Number>1333-74-0</CAS_Number>
      <Formula>H2</Formula>
      <SMILES>[H][H]</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>2.01588</Molar_Weight>
      <Critical_Temperature>33.19</Critical_Temperature>
      <Critical_Pressure>1313000</Critical_Pressure>
      <Critical_Volume>0.064147</Critical_Volume>
      <Critical_Compressibility>0.305</Critical_Compressibility>
      <Acentric_Factor>-0.215993</Acentric_Factor>
      <Z_Rackett>0.3139</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.00158781835225</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>31</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>64.7712165406671</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>0</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>0</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>13.05</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-97.534</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>1.0355</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>0.00031816</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>13.08</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>33.19</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>3994.325</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-48.69006</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>10.36209</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.000340144</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.960333E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-32.531</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>97.304</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>5.9178</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-0.0031563</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>2.9613</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.25981</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>33.19</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.19104</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>13.84</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>33.18</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>14510</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-1191.1</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>156.51</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-6.1773</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.087907</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>13.84</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>32</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.34238</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-4.3002</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-0.53814</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0.0011639</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-0.00021792</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>13.84</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>31</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0.0026851</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.74366</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>13.289</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-31.305</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>10</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1600</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>1.7916E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.68557</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>-0.51413</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>132.61</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>13.95</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>2000</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>-0.003232</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>1.9865</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-5.0915</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>-0.00046122</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-0.00062971</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>13.95</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>32.18</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>5730</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-1.3847E-11</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>1.1605E-12</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-1.2321E-13</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>4.114E-15</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>13.95</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>23.45</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>20.39</Normal_Boiling_Point>
      <ID>902</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>1534700</HVap_A>
      <HVap_B>3.214</HVap_B>
      <HVap_C>-8.4567</HVap_C>
      <HVap_D>8.4646</HVap_D>
      <HVap_TMIN>13.95</HVap_TMIN>
      <HVap_TMAX>32.62</HVap_TMAX>
      <UNIQUAC_R>0.4092</UNIQUAC_R>
      <UNIQUAC_Q>0.5516</UNIQUAC_Q>
      <IsFPROPSSupported>true</IsFPROPSSupported>
      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation>101</VaporPressureEquation>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
      <SurfaceTensionEquation>16</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>ChemSep</OriginalDB>
      <CurrentDB>ChemSep</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName></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>13.95</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0.1171</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 />
      <MODFACGroups />
      <Elements />
    </Compound>
  </Compounds>
  <ReactionSets>
    <ReactionSet>
      <ID>DefaultSet</ID>
      <Name>Default Set</Name>
      <Description>Default Reaction Set</Description>
      <Reactions>
        <Reaction Key="bdddf5ee-6f42-4899-9bde-0f2cdf0a8cee" ReactionID="bdddf5ee-6f42-4899-9bde-0f2cdf0a8cee" Rank="0" IsActive="true" />
      </Reactions>
    </ReactionSet>
  </ReactionSets>
  <Reactions>
    <Reaction>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Reaction</Type>
      <StoichBalance>0</StoichBalance>
      <ReactionHeatCO>0</ReactionHeatCO>
      <ReactionHeat>124910</ReactionHeat>
      <Equation>CH3CH2CH3 --&gt; CH2CHCH3 + H2 </Equation>
      <Name>hydrogenation</Name>
      <ID>bdddf5ee-6f42-4899-9bde-0f2cdf0a8cee</ID>
      <Description></Description>
      <BaseReactant>Propane</BaseReactant>
      <ReactionPhase>Vapor</ReactionPhase>
      <ReactionType>Conversion</ReactionType>
      <ReactionBasis>MolarConc</ReactionBasis>
      <Kvalue>0</Kvalue>
      <ReactionGibbsEnergy>0</ReactionGibbsEnergy>
      <ConstantKeqValue>0</ConstantKeqValue>
      <Tmax>0</Tmax>
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      &lt;Contents Count="2"&gt;
        &lt;Content ID="0" RefID="2" /&gt;
        &lt;Content ID="1" RefID="3" /&gt;
      &lt;/Contents&gt;
    &lt;/Pane&gt;
    &lt;Pane ID="3" DockState="Document" ActiveContent="6"&gt;
      &lt;Contents Count="3"&gt;
        &lt;Content ID="0" RefID="4" /&gt;
        &lt;Content ID="1" RefID="5" /&gt;
        &lt;Content ID="2" RefID="6" /&gt;
      &lt;/Contents&gt;
    &lt;/Pane&gt;
  &lt;/Panes&gt;
  &lt;DockWindows&gt;
    &lt;DockWindow ID="0" DockState="Document" ZOrderIndex="1"&gt;
      &lt;NestedPanes Count="1"&gt;
        &lt;Pane ID="0" RefID="3" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
      &lt;/NestedPanes&gt;
    &lt;/DockWindow&gt;
    &lt;DockWindow ID="1" DockState="DockLeft" ZOrderIndex="5"&gt;
      &lt;NestedPanes Count="1"&gt;
        &lt;Pane ID="0" RefID="2" 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="1"&gt;
        &lt;Pane ID="0" RefID="1" PrevPane="-1" Alignment="Bottom" Proportion="0.5" /&gt;
      &lt;/NestedPanes&gt;
    &lt;/DockWindow&gt;
    &lt;DockWindow ID="3" DockState="DockTop" ZOrderIndex="6"&gt;
      &lt;NestedPanes Count="0" /&gt;
    &lt;/DockWindow&gt;
    &lt;DockWindow ID="4" DockState="DockBottom" ZOrderIndex="3"&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;/DockWindows&gt;
  &lt;FloatWindows Count="0" /&gt;
&lt;/DockPanel&gt;</PanelLayout>
</DWSIM_Simulation_Data>