<?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 8.1 Single Language, Version 6.2.9200.0, Win32NT Platform</OSInfo>
    <SavedOn>2015-03-05T18:06:01.9630925+05:30</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>DELL-PC\dell</SimAutor>
    <SimComentario>simulation_details</SimComentario>
    <FilePath>E:\microsoft\dwsim problems\chapter 4\dwsim483.dwxml</FilePath>
    <BackupFileName>89316893.dwbcs</BackupFileName>
    <CalculatorActivated>true</CalculatorActivated>
    <PropertyPackageFlashAlgorithm>DWSIMDefault</PropertyPackageFlashAlgorithm>
    <PropertyPackageIOFlashQuickMode>true</PropertyPackageIOFlashQuickMode>
    <ThreePhaseFlashStabTestSeverity>0</ThreePhaseFlashStabTestSeverity>
    <FlashValidationDGETolerancePct>0.01</FlashValidationDGETolerancePct>
    <Password></Password>
    <UsePassword>false</UsePassword>
    <ThreePhaseFlashStabTestCompIds>Ethane,Oxygen,Nitrogen,Carbon monoxide,Carbon dioxide,Water</ThreePhaseFlashStabTestCompIds>
  </Settings>
  <SimulationObjects>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Ethane</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-aff66e12-321e-41d9-a6f9-3b2bb86256c2</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-aff66e12-321e-41d9-a6f9-3b2bb86256c2</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-e4cbc096-b01c-4ab5-92f7-7a7fb38c98b3</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0384615384615385</FracaoMolar>
              <FracaoMassica>0.0400217610839283</FracaoMassica>
              <MolarFlow>100</MolarFlow>
              <MassFlow>3.007</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.201923076923077</FracaoMolar>
              <FracaoMassica>0.223593140932965</FracaoMassica>
              <MolarFlow>525</MolarFlow>
              <MassFlow>16.799475</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.759615384615385</FracaoMolar>
              <FracaoMassica>0.736385097983107</FracaoMassica>
              <MolarFlow>1975</MolarFlow>
              <MassFlow>55.32765</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>-518.400050853166</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>2600</molarflow>
            <massflow>75.134125</massflow>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>28.8977403846154</molecularWeight>
            <pressure>506625</pressure>
            <temperature>1000</temperature>
            <thermalConductivity>-0.200081831805362</thermalConductivity>
            <volumetric_flow>-0.144934640489226</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>0</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>0.0384615384615385</FracaoMolar>
              <FracaoMassica>0.0400217610839283</FracaoMassica>
              <MolarFlow>100</MolarFlow>
              <MassFlow>3.007</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.201923076923077</FracaoMolar>
              <FracaoMassica>0.223593140932965</FracaoMassica>
              <MolarFlow>525</MolarFlow>
              <MassFlow>16.799475</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.759615384615385</FracaoMolar>
              <FracaoMassica>0.736385097983107</FracaoMassica>
              <MolarFlow>1975</MolarFlow>
              <MassFlow>55.32765</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>-518.400050853166</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>2600</molarflow>
            <massflow>75.134125</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>28.8977403846154</molecularWeight>
            <thermalConductivity>-0.200081831805362</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>0</kinematic_viscosity>
            <volumetric_flow>0</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>0.0384615384615385</FracaoMolar>
              <FracaoMassica>0.0400217610839283</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00185756480373</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.201923076923077</FracaoMolar>
              <FracaoMassica>0.223593140932965</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00106513996287</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.759615384615385</FracaoMolar>
              <FracaoMassica>0.736385097983107</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00141880290322</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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>1.00144450840975</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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>1.00128656827923</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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>1.00026647471878</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0384615384615385</FracaoMolar>
              <FracaoMassica>0.0400217610839283</FracaoMassica>
              <MolarFlow>100</MolarFlow>
              <MassFlow>3.007</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.201923076923077</FracaoMolar>
              <FracaoMassica>0.223593140932965</FracaoMassica>
              <MolarFlow>525</MolarFlow>
              <MassFlow>16.799475</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.759615384615385</FracaoMolar>
              <FracaoMassica>0.736385097983107</FracaoMassica>
              <MolarFlow>1975</MolarFlow>
              <MassFlow>55.32765</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>-0.00339684277853176</compressibilityFactor>
            <density>-518.400050853166</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>2600</molarflow>
            <massflow>75.134125</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>28.8977403846154</molecularWeight>
            <thermalConductivity>-0.200081831805362</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>0</kinematic_viscosity>
            <volumetric_flow>-0.144934640489226</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>
              <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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</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>
              <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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>NaN</DeltaQ>
      <ScriptExt_FontName>Courier New</ScriptExt_FontName>
      <ScriptExt_FontSize>10</ScriptExt_FontSize>
      <ScriptExt_ScriptTextB></ScriptExt_ScriptTextB>
      <ScriptExt_ScriptTextA></ScriptExt_ScriptTextA>
      <ScriptExt_Language>IronPython</ScriptExt_Language>
      <ErrorMessage></ErrorMessage>
      <ComponentDescription>ReatorConversao</ComponentDescription>
      <ComponentName>RC-79229e27-06f8-4093-b54d-16f97d93bce0</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-79229e27-06f8-4093-b54d-16f97d93bce0</Nome>
      <ShowQuickTable>false</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
      <ReactionSequence>
        <Item Index="0">1080a25e-de78-4d5c-9d21-7ffb013e6b98,d25c4062-c4e6-4653-b1a6-1127ced99573</Item>
      </ReactionSequence>
      <Reactions />
      <ReactionConversions>
        <Reaction ID="1080a25e-de78-4d5c-9d21-7ffb013e6b98">0.65</Reaction>
        <Reaction ID="d25c4062-c4e6-4653-b1a6-1127ced99573">0.25</Reaction>
      </ReactionConversions>
      <CompoundConversions />
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Flows</CompositionBasis>
      <ComponentDescription>MAT-c27d26b9-a32c-409c-b5a4-7aad7c8c306b</ComponentDescription>
      <ComponentName>liquid</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-c27d26b9-a32c-409c-b5a4-7aad7c8c306b</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-e4cbc096-b01c-4ab5-92f7-7a7fb38c98b3</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00992204110559887</FracaoMolar>
              <FracaoMassica>0.0105057380650331</FracaoMassica>
              <MolarFlow>26.2500644162107</MolarFlow>
              <MassFlow>0.789339436995456</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.104181431608788</FracaoMolar>
              <FracaoMassica>0.117386687050264</FracaoMassica>
              <MolarFlow>275.625676370212</MolarFlow>
              <MassFlow>8.81974601817042</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.746515473659343</FracaoMolar>
              <FracaoMassica>0.736386905035969</FracaoMassica>
              <MolarFlow>1975.004846553</MolarFlow>
              <MassFlow>55.3277857713356</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00661469407039925</FracaoMolar>
              <FracaoMassica>0.0065240155903243</FracaoMassica>
              <MolarFlow>17.5000429441405</MolarFlow>
              <MassFlow>0.490176202865375</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0491377273801087</FracaoMolar>
              <FracaoMassica>0.0761471440524487</FracaoMassica>
              <MolarFlow>130.000319013615</MolarFlow>
              <MassFlow>5.72124903962969</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>1</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0836286321757619</FracaoMolar>
              <FracaoMassica>0.053049510205961</FracaoMassica>
              <MolarFlow>221.250542936633</MolarFlow>
              <MassFlow>3.98582853100345</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>-530.778256090463</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>2645.63149223381</molarflow>
            <massflow>75.134125</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>28.3993160878809</molecularWeight>
            <pressure>506625</pressure>
            <temperature>1000</temperature>
            <thermalConductivity>-0.219348660548514</thermalConductivity>
            <volumetric_flow>-0.141554640074017</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>0.00992204110559887</FracaoMolar>
              <FracaoMassica>0.0105057380650331</FracaoMassica>
              <MolarFlow>26.2500644162107</MolarFlow>
              <MassFlow>0.789339436995456</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.104181431608788</FracaoMolar>
              <FracaoMassica>0.117386687050264</FracaoMassica>
              <MolarFlow>275.625676370212</MolarFlow>
              <MassFlow>8.81974601817042</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.746515473659343</FracaoMolar>
              <FracaoMassica>0.736386905035969</FracaoMassica>
              <MolarFlow>1975.004846553</MolarFlow>
              <MassFlow>55.3277857713356</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00661469407039925</FracaoMolar>
              <FracaoMassica>0.0065240155903243</FracaoMassica>
              <MolarFlow>17.5000429441405</MolarFlow>
              <MassFlow>0.490176202865375</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0491377273801087</FracaoMolar>
              <FracaoMassica>0.0761471440524487</FracaoMassica>
              <MolarFlow>130.000319013615</MolarFlow>
              <MassFlow>5.72124903962969</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0836286321757619</FracaoMolar>
              <FracaoMassica>0.053049510205961</FracaoMassica>
              <MolarFlow>221.250542936633</MolarFlow>
              <MassFlow>3.98582853100345</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>-530.778256090463</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>2645.63149223381</molarflow>
            <massflow>75.134125</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>28.3993160878809</molecularWeight>
            <thermalConductivity>-0.219348660548514</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>0</kinematic_viscosity>
            <volumetric_flow>0</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>0.00992204110559887</FracaoMolar>
              <FracaoMassica>0.0105057380650331</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00169629389413</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.104181431608788</FracaoMolar>
              <FracaoMassica>0.117386687050264</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00105734623624</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.746515473659343</FracaoMolar>
              <FracaoMassica>0.736386905035969</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00144258303944</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00661469407039925</FracaoMolar>
              <FracaoMassica>0.0065240155903243</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00146543206553</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0491377273801087</FracaoMolar>
              <FracaoMassica>0.0761471440524487</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00120456195166</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0836286321757619</FracaoMolar>
              <FracaoMassica>0.053049510205961</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1.00000689772073</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00992204110559887</FracaoMolar>
              <FracaoMassica>0.0105057380650331</FracaoMassica>
              <MolarFlow>26.2500644162107</MolarFlow>
              <MassFlow>0.789339436995456</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.104181431608788</FracaoMolar>
              <FracaoMassica>0.117386687050264</FracaoMassica>
              <MolarFlow>275.625676370212</MolarFlow>
              <MassFlow>8.81974601817042</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.746515473659343</FracaoMolar>
              <FracaoMassica>0.736386905035969</FracaoMassica>
              <MolarFlow>1975.004846553</MolarFlow>
              <MassFlow>55.3277857713356</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.00661469407039925</FracaoMolar>
              <FracaoMassica>0.0065240155903243</FracaoMassica>
              <MolarFlow>17.5000429441405</MolarFlow>
              <MassFlow>0.490176202865375</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0491377273801087</FracaoMolar>
              <FracaoMassica>0.0761471440524487</FracaoMassica>
              <MolarFlow>130.000319013615</MolarFlow>
              <MassFlow>5.72124903962969</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0836286321757619</FracaoMolar>
              <FracaoMassica>0.053049510205961</FracaoMassica>
              <MolarFlow>221.250542936633</MolarFlow>
              <MassFlow>3.98582853100345</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>-0.00326040353146102</compressibilityFactor>
            <density>-530.778256090463</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>2645.63149223381</molarflow>
            <massflow>75.134125</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>28.3993160878809</molecularWeight>
            <thermalConductivity>-0.219348660548514</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>0</kinematic_viscosity>
            <volumetric_flow>-0.141554640074017</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>
              <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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</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>
              <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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-8b4643bd-1a86-4c3f-8d02-bf42c965a017</ComponentDescription>
      <ComponentName>vapor</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-8b4643bd-1a86-4c3f-8d02-bf42c965a017</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-e4cbc096-b01c-4ab5-92f7-7a7fb38c98b3</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>506625</pressure>
            <temperature>1000</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>
              <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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</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>
              <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>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxygen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Nitrogen</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon monoxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Carbon dioxide</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</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Water</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>Ethane</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>Oxygen</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>Nitrogen</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>Carbon monoxide</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>Carbon dioxide</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>Water</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>NaN</Energia>
      <ComponentDescription>EN-f8ce2f81-a41f-4185-8ee3-78c441714bc1</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-f8ce2f81-a41f-4185-8ee3-78c441714bc1</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
    </SimulationObject>
  </SimulationObjects>
  <GraphicObjects>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>feed</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5034</X>
      <Y>3594</Y>
      <Name>MAT-aff66e12-321e-41d9-a6f9-3b2bb86256c2</Name>
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      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="False" />
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      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="RC-79229e27-06f8-4093-b54d-16f97d93bce0" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.ReactorConversionGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>true</SplitPoint>
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      <Description>ReatorConversao</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>RCT_Conversion</TipoObjeto>
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      <Calculated>true</Calculated>
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      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="MAT-c27d26b9-a32c-409c-b5a4-7aad7c8c306b" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="MAT-8b4643bd-1a86-4c3f-8d02-bf42c965a017" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>liquid</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5292</X>
      <Y>3561</Y>
      <Name>MAT-c27d26b9-a32c-409c-b5a4-7aad7c8c306b</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="RC-79229e27-06f8-4093-b54d-16f97d93bce0" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>vapor</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5305</X>
      <Y>3624</Y>
      <Name>MAT-8b4643bd-1a86-4c3f-8d02-bf42c965a017</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="RC-79229e27-06f8-4093-b54d-16f97d93bce0" AttachedFromConnIndex="1" AttachedFromEnergyConn="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.EnergyStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>LightYellow</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Correntedeenergia</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>EnergyStream</TipoObjeto>
      <IsEnergyStream>true</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>e1</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5023</X>
      <Y>3669</Y>
      <Name>EN-f8ce2f81-a41f-4185-8ee3-78c441714bc1</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
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        <Connector IsAttached="False" />
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      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="RC-79229e27-06f8-4093-b54d-16f97d93bce0" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
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      <SpecialConnectors />
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  </GraphicObjects>
  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-e4cbc096-b01c-4ab5-92f7-7a7fb38c98b3</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>Ethane,Oxygen,Nitrogen,Carbon monoxide,Carbon dioxide,Water</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="Nitrogen" Compound2="Carbon monoxide" Value="0.033" />
        <InteractionParameter Compound1="Nitrogen" Compound2="Oxygen" Value="-0.0159" />
        <InteractionParameter Compound1="Nitrogen" Compound2="Ethane" Value="0.0344" />
        <InteractionParameter Compound1="Nitrogen" Compound2="Carbon dioxide" Value="-0.0222" />
        <InteractionParameter Compound1="Carbon monoxide" Compound2="Ethane" Value="-0.0226" />
        <InteractionParameter Compound1="Carbon dioxide" Compound2="Ethane" Value="0.1326" />
        <InteractionParameter Compound1="Carbon dioxide" Compound2="Water" Value="0.0063" />
      </InteractionParameters>
    </PropertyPackage>
  </PropertyPackages>
  <Compounds>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Ethane</Name>
      <CAS_Number>74-84-0</CAS_Number>
      <Formula>CH3CH3</Formula>
      <SMILES>CC</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>30.07</Molar_Weight>
      <Critical_Temperature>305.32</Critical_Temperature>
      <Critical_Pressure>4872000</Critical_Pressure>
      <Critical_Volume>0.1455</Critical_Volume>
      <Critical_Compressibility>0.279</Critical_Compressibility>
      <Acentric_Factor>0.099</Acentric_Factor>
      <Z_Rackett>0.2793</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.0908</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.0029557670192</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>55.1979</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>7.61955437312936</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-2787.49584303292</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-1061.52311273695</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>59.627</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-2798.1</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-6.4341</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>1.8742E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>90.35</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>305.42</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>35666.22</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-616.5198</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>11.69914</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>0.000444525</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>-1.541942E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-15.914</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>421.54</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>1.0503</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-1.6719E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>1.3749</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.23949</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>305.43</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.22875</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>88.71</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>305.42</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>68726</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-1953.6</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>31.772</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-0.10571</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.00019673</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>88.71</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>290</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.073876</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-9.6787</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-0.67405</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.003407</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-2.2023E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>90.35</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>300</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>7.4549E-05</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>1.168</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>506.4</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-881.74</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>184.55</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1000</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>5.2452E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.58906</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>188.8</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>-2953.8</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>90.35</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>25.301</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.012024</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>90.35</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.0092564</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>30.13</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-3.5743</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.0026003</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-2.1736E-05</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>89.88</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>305.32</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>7021.9</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-1326.3</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>90.192</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-1.4782</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.0082308</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>15.53</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>78.55</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>184.55</Normal_Boiling_Point>
      <ID>2</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>23996000</HVap_A>
      <HVap_B>1.4625</HVap_B>
      <HVap_C>-2.8991</HVap_C>
      <HVap_D>2.8421</HVap_D>
      <HVap_TMIN>89.88</HVap_TMIN>
      <HVap_TMAX>305.33</HVap_TMAX>
      <UNIQUAC_R>1.8022</UNIQUAC_R>
      <UNIQUAC_Q>1.696</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>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>90.352</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>2.859</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="CH3" Value="2" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH3" Value="2" />
      </MODFACGroups>
      <Elements />
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Oxygen</Name>
      <CAS_Number>7782-44-7</CAS_Number>
      <Formula>O2</Formula>
      <SMILES>O=O</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>31.999</Molar_Weight>
      <Critical_Temperature>154.58</Critical_Temperature>
      <Critical_Pressure>5043000</Critical_Pressure>
      <Critical_Volume>0.07337</Critical_Volume>
      <Critical_Compressibility>0.288</Critical_Compressibility>
      <Acentric_Factor>0.022</Acentric_Factor>
      <Z_Rackett>0.2908</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.019</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.00195422125278</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>28.0225</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>6.4077939935623</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>45.477</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-1192.8</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-4.7115</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>5.953E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>54.35</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>154.8</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>29061.62</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-1470.897</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>11.10778</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.00128484</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>3.183122E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-5.2319</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>116.13</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-1.0315</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>3.4376E-06</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>2.6097</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.23614</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>154.78</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.23695</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>54.35</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>154.77</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>53393</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-1966.4</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>48.21</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-0.31631</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.0010466</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>54.36</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>145</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.19654</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-10.535</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-0.46717</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.0052064</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-3.3418E-07</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>50</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>150</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0.0004508</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.74544</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>58.278</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-562.62</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>60</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>2000</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>8.0134E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.60321</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>56.09</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>1584.9</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>54.35</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1950</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>44.552</Solid_Density_Const_A>
      <Solid_Density_Const_B>-4.4857E-08</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>20.65</Solid_Density_Tmin>
      <Solid_Density_Tmax>30.15</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.0062662</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>17.53</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-3.9173</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.0058473</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-9.1613E-05</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>54.35</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>154.58</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>-15381</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>1601.9</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>-10.968</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0.24187</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>-0.0020734</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>13.46</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>43.78</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>90.17</Normal_Boiling_Point>
      <ID>901</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>10672000</HVap_A>
      <HVap_B>1.5661</HVap_B>
      <HVap_C>-3.4356</HVap_C>
      <HVap_D>3.5416</HVap_D>
      <HVap_TMIN>54.36</HVap_TMIN>
      <HVap_TMAX>154.58</HVap_TMAX>
      <UNIQUAC_R>0.857</UNIQUAC_R>
      <UNIQUAC_Q>0.94</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>54.361</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0.444</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>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Nitrogen</Name>
      <CAS_Number>7727-37-9</CAS_Number>
      <Formula>N2</Formula>
      <SMILES>N#N</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>28.014</Molar_Weight>
      <Critical_Temperature>126.2</Critical_Temperature>
      <Critical_Pressure>3398000</Critical_Pressure>
      <Critical_Volume>0.0901</Critical_Volume>
      <Critical_Compressibility>0.289</Critical_Compressibility>
      <Acentric_Factor>0.037</Acentric_Factor>
      <Z_Rackett>0.2906</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.045</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.00216918504124</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>34.6723</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>6.83586778039552</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>40.523</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-943.5</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-3.9646</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>7.3431E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>60.81</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>126.26</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>29103.63</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-2305.946</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>11.31935</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.00100557</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.706099E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>3.4358</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>-24.706</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-2.6748</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-4.1603E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>2.435</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.25137</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>126.27</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.249</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>63.15</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>126.26</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>55135</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>217.45</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>-0.9071</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0.05327</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.00024166</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>63.15</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>115</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.21743</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>10.383</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-1.0631</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0.00036245</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-2.3265E-05</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>60</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>124</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0.0003395</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.76921</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>19.592</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>293.93</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>50</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>2000</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>4.6051E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.65049</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>5.8019</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>2822.7</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>63.15</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1970</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>37.87</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.06027</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>20.65</Solid_Density_Tmin>
      <Solid_Density_Tmax>63.15</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.0025409</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>96.836</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-7.6473</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.05313</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-0.00036553</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>63.15</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>126.2</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>383890</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-28798</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>875.74</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-11.589</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.057106</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>32.8</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>63</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>77.35</Normal_Boiling_Point>
      <ID>905</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>27284000</HVap_A>
      <HVap_B>7.8021</HVap_B>
      <HVap_C>-19.125</HVap_C>
      <HVap_D>19.518</HVap_D>
      <HVap_TMIN>63.15</HVap_TMIN>
      <HVap_TMAX>126.26</HVap_TMAX>
      <UNIQUAC_R>1.0415</UNIQUAC_R>
      <UNIQUAC_Q>1.088</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>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>63.149</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0.72</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>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Carbon monoxide</Name>
      <CAS_Number>630-08-0</CAS_Number>
      <Formula>CO</Formula>
      <SMILES>[C+]#[O-]</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>28.01</Molar_Weight>
      <Critical_Temperature>132.85</Critical_Temperature>
      <Critical_Pressure>3494000</Critical_Pressure>
      <Critical_Volume>0.0931</Critical_Volume>
      <Critical_Compressibility>0.292</Critical_Compressibility>
      <Acentric_Factor>0.045</Acentric_Factor>
      <Z_Rackett>0.2918</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.093</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.00152917807656</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>35.4426</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>7.05305248125669</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-3946.09068189932</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-4896.46554801856</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>3.74E-31</Dipole_Moment>
      <Vapor_Pressure_Constant_A>42.283</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-1035.1</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-4.2012</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>6.2546E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>64.07</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>132.92</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>29100</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-1979.753</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>10.58274</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-7.90406E-05</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>-1.99685E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-82.158</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>1037.8</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>14.229</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-0.00028204</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>2.2423</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.2437</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>132.93</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.24196</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>68.13</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>132.92</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>63364</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-10524</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>359.6</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-3.9494</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.014624</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>68.09</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>132</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.23621</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-3.5251</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-0.55788</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.0039362</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-8.2725E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>65</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>125</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0.00061581</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.6828</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>61.287</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>221.32</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>70</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1500</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>1.2713E-06</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.51494</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>105.97</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>-231.11</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>68.15</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1273.15</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>38.293</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.062464</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>27.26</Solid_Density_Tmin>
      <Solid_Density_Tmax>68.15</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.0087233</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>5.9843</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-3.6585</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.00036163</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-6.7401E-05</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>68.15</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>129.51</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>-1396</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-235.75</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>86.77</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-2.1914</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.018145</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>11.95</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>62</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>81.66</Normal_Boiling_Point>
      <ID>908</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>8585000</HVap_A>
      <HVap_B>0.4921</HVap_B>
      <HVap_C>-0.326</HVap_C>
      <HVap_D>0.2231</HVap_D>
      <HVap_TMIN>68.13</HVap_TMIN>
      <HVap_TMAX>132.5</HVap_TMAX>
      <UNIQUAC_R>1.0679</UNIQUAC_R>
      <UNIQUAC_Q>1.112</UNIQUAC_Q>
      <IsFPROPSSupported>true</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>68.15</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0.840984</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>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Carbon dioxide</Name>
      <CAS_Number>124-38-9</CAS_Number>
      <Formula>OCO</Formula>
      <SMILES>O=C=O</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>44.0095</Molar_Weight>
      <Critical_Temperature>304.21</Critical_Temperature>
      <Critical_Pressure>7383000</Critical_Pressure>
      <Critical_Volume>0.094</Critical_Volume>
      <Critical_Compressibility>0.274</Critical_Compressibility>
      <Acentric_Factor>0.223621</Acentric_Factor>
      <Z_Rackett>0.270937</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.231</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.0034785053748</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>37.2744</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>4.85524716254445</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-8941.47854440518</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-8961.01977982027</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>95.478</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-4070</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-12.07</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>2.9505E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>216.4</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>304.21</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>28933</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-494.28</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>10.658</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-2.7375E-05</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>3.3268E-09</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-7.7022</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>-166.34</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>0.38094</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-4.018E-05</Liquid_Viscosity_Const_D>
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      <Liquid_Density_Const_A>2.768</Liquid_Density_Const_A>
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      <Liquid_Heat_Capacity_Const_A>80592</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>108.83</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>-6.9126</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0.059647</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>6.9922E-06</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>216.58</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>290</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.24975</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-55.106</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0.41735</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.0051067</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>2.0157E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>216.58</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>300</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>5.804</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>-0.44522</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>794.13</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>2139600</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>180</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1500</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>2.2464E-06</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.45495</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>292.64</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>1669.1</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>170</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1900</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>42.04</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.034421</Solid_Density_Const_B>
      <Solid_Density_Const_C>-0.0002847</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>143.1</Solid_Density_Tmin>
      <Solid_Density_Tmax>216.58</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.011629</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>-183.67</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0.069773</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>-0.012408</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-1.8232E-06</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>216.58</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>304.21</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>-18283</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>1360.3</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>-12.153</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0.051584</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>-7.6997E-05</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>25</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>216.58</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>0</Normal_Boiling_Point>
      <ID>909</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>21092000</HVap_A>
      <HVap_B>0.35366</HVap_B>
      <HVap_C>-0.46134</HVap_C>
      <HVap_D>0.43554</HVap_D>
      <HVap_TMIN>216.58</HVap_TMIN>
      <HVap_TMAX>304.21</HVap_TMAX>
      <UNIQUAC_R>1.2986</UNIQUAC_R>
      <UNIQUAC_Q>1.292</UNIQUAC_Q>
      <IsFPROPSSupported>true</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>216.58</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>9.019</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>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Water</Name>
      <CAS_Number>7732-18-5</CAS_Number>
      <Formula>HOH</Formula>
      <SMILES>O</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>18.015</Molar_Weight>
      <Critical_Temperature>647.14</Critical_Temperature>
      <Critical_Pressure>22064000</Critical_Pressure>
      <Critical_Volume>0.05595</Critical_Volume>
      <Critical_Compressibility>0.229</Critical_Compressibility>
      <Acentric_Factor>0.344</Acentric_Factor>
      <Z_Rackett>0.2338</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.328</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.0114198721442</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>18.0674</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>10.4759367194005</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-13422.9253399944</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-12688.8703857896</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>6.17E-30</Dipole_Moment>
      <Vapor_Pressure_Constant_A>98.515</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-8530.7</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-10.984</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>6.3663E-06</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>263.15</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>647.29</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>33200</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-878.9001</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>8.436956</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>0.00207627</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>-6.467085E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-133.7</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>6785.7</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>18.47</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-1.4736E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>32.51621</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>-3.213004</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>7.92411</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>-7.359898</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>2.703522</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>253.1</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>647.29</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>75539</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-22297</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>136.02</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-0.25622</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.00018273</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>273.1</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>533.15</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-1.5697</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-55.141</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0.7832</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0.0011484</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-1.8151E-06</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>273.1</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>633.15</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>6.5986E-06</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>1.3947</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>59.478</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-15484</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>273.16</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1073.15</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>7.002327E-08</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.934576</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>195.6338</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>-13045.99</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>273.16</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1073.15</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>52.967</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.0075822</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>233.15</Solid_Density_Tmin>
      <Solid_Density_Tmax>273.15</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.031819</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>167.09</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-3.6781</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.0053717</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-8.4188E-06</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>265.1</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>647.1</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>-262.51</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>140.52</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>-3.8869E-06</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-1.1996E-08</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>7.1879E-11</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>3.15</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>273.15</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>373.15</Normal_Boiling_Point>
      <ID>1921</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>59640000</HVap_A>
      <HVap_B>0.86515</HVap_B>
      <HVap_C>-1.1134</HVap_C>
      <HVap_D>0.67764</HVap_D>
      <HVap_TMIN>273.15</HVap_TMIN>
      <HVap_TMAX>647.28</HVap_TMAX>
      <UNIQUAC_R>0.92</UNIQUAC_R>
      <UNIQUAC_Q>1.4</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>106</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>273.15</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>6.00174</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="H2O" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="H2O" Value="1" />
      </MODFACGroups>
      <Elements />
    </Compound>
  </Compounds>
  <ReactionSets>
    <ReactionSet>
      <ID>DefaultSet</ID>
      <Name>Default Set</Name>
      <Description>Default Reaction Set</Description>
      <Reactions>
        <Reaction Key="1080a25e-de78-4d5c-9d21-7ffb013e6b98" ReactionID="1080a25e-de78-4d5c-9d21-7ffb013e6b98" Rank="0" IsActive="true" />
        <Reaction Key="d25c4062-c4e6-4653-b1a6-1127ced99573" ReactionID="d25c4062-c4e6-4653-b1a6-1127ced99573" Rank="0" IsActive="true" />
      </Reactions>
    </ReactionSet>
  </ReactionSets>
  <Reactions>
    <Reaction>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Reaction</Type>
      <StoichBalance>0</StoichBalance>
      <ReactionHeatCO>0</ReactionHeatCO>
      <ReactionHeat>-1428642</ReactionHeat>
      <Equation>CH3CH3 + 3.5O2 --&gt; 2OCO + 3HOH </Equation>
      <Name></Name>
      <ID>1080a25e-de78-4d5c-9d21-7ffb013e6b98</ID>
      <Description></Description>
      <BaseReactant>Ethane</BaseReactant>
      <ReactionPhase>Mixture</ReactionPhase>
      <ReactionType>Conversion</ReactionType>
      <ReactionBasis>MolarConc</ReactionBasis>
      <Kvalue>0</Kvalue>
      <ReactionGibbsEnergy>0</ReactionGibbsEnergy>
      <ConstantKeqValue>0</ConstantKeqValue>
      <Tmax>0</Tmax>
      <Tmin>0</Tmin>
      <Approach>0</Approach>
      <Expression>65</Expression>
      <KExprType>Gibbs</KExprType>
      <Rate>0</Rate>
      <VelUnit>mol/[m3.s]</VelUnit>
      <ConcUnit>mol/m3</ConcUnit>
      <A_Forward>0</A_Forward>
      <A_Reverse>0</A_Reverse>
      <E_Forward>0</E_Forward>
      <E_Reverse>0</E_Reverse>
      <Compounds>
        <Compound Name="Ethane" StoichCoeff="-1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="true" />
        <Compound Name="Oxygen" StoichCoeff="-3.5" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Carbon dioxide" StoichCoeff="2" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Water" StoichCoeff="3" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
      </Compounds>
    </Reaction>
    <Reaction>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Reaction</Type>
      <StoichBalance>0</StoichBalance>
      <ReactionHeatCO>0</ReactionHeatCO>
      <ReactionHeat>-862682</ReactionHeat>
      <Equation>CH3CH3 + 2.5O2 --&gt; 2CO + 3HOH </Equation>
      <Name></Name>
      <ID>d25c4062-c4e6-4653-b1a6-1127ced99573</ID>
      <Description></Description>
      <BaseReactant>Ethane</BaseReactant>
      <ReactionPhase>Mixture</ReactionPhase>
      <ReactionType>Conversion</ReactionType>
      <ReactionBasis>MolarConc</ReactionBasis>
      <Kvalue>0</Kvalue>
      <ReactionGibbsEnergy>0</ReactionGibbsEnergy>
      <ConstantKeqValue>0</ConstantKeqValue>
      <Tmax>0</Tmax>
      <Tmin>0</Tmin>
      <Approach>0</Approach>
      <Expression>25</Expression>
      <KExprType>Gibbs</KExprType>
      <Rate>0</Rate>
      <VelUnit>mol/[m3.s]</VelUnit>
      <ConcUnit>mol/m3</ConcUnit>
      <A_Forward>0</A_Forward>
      <A_Reverse>0</A_Reverse>
      <E_Forward>0</E_Forward>
      <E_Reverse>0</E_Reverse>
      <Compounds>
        <Compound Name="Ethane" StoichCoeff="-1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="true" />
        <Compound Name="Oxygen" StoichCoeff="-2.5" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Carbon monoxide" StoichCoeff="2" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Water" StoichCoeff="3" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
      </Compounds>
    </Reaction>
  </Reactions>
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  <SensitivityAnalysis />
  <PetroleumAssays />
  <WatchItems />
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