<?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>2014-12-13T17:28:36.0520861+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>H:\dwsim941.dwxml</FilePath>
    <BackupFileName>52134353.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,Ethylene,Hydrogen</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-35b18644-de72-439c-905f-74a6b6cdcbc1</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-35b18644-de72-439c-905f-74a6b6cdcbc1</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-385a746d-d3b1-4e06-9402-5f054f64d7d2</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>1</FracaoMolar>
              <FracaoMassica>1</FracaoMassica>
              <MolarFlow>1</MolarFlow>
              <MassFlow>0.03007</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>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>1.23965669980455</density>
            <enthalpy>-1.9684272155546</enthalpy>
            <entropy>-0.00426388637961189</entropy>
            <molarflow>1</molarflow>
            <massflow>0.03007</massflow>
            <heatCapacityCp>1.76604625792183</heatCapacityCp>
            <heatCapacityCv>1.47826868044492</heatCapacityCv>
            <molecularWeight>30.07</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.0215309297002463</thermalConductivity>
            <volumetric_flow>0.0242567155929064</volumetric_flow>
            <molar_enthalpy>-59.1906063717268</molar_enthalpy>
            <molar_entropy>-0.128215063434929</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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>1</FracaoMolar>
              <FracaoMassica>1</FracaoMassica>
              <MolarFlow>1</MolarFlow>
              <MassFlow>0.03007</MassFlow>
              <FugacityCoeff>0.991578694998487</FugacityCoeff>
              <ActivityCoeff>0.0239537923304926</ActivityCoeff>
              <PartialVolume>0.024256714289203</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.0242567155929064</VolumetricFlow>
              <VolumetricFraction>1</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>0.993817080294112</FugacityCoeff>
              <ActivityCoeff>0.0143207168363924</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethylene</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>1.00659906200479</FugacityCoeff>
              <ActivityCoeff>4.34473714225928E-16</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.991525241777926</compressibilityFactor>
            <density>1.23965669980455</density>
            <enthalpy>-1.9684272155546</enthalpy>
            <entropy>-0.00426388637961189</entropy>
            <molarflow>1</molarflow>
            <massflow>0.03007</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>1.76604625792183</heatCapacityCp>
            <heatCapacityCv>1.47826868044492</heatCapacityCv>
            <molecularWeight>30.07</molecularWeight>
            <thermalConductivity>0.0215309297002463</thermalConductivity>
            <viscosity>9.68534590871701E-06</viscosity>
            <kinematic_viscosity>7.81292587717553E-06</kinematic_viscosity>
            <volumetric_flow>0.0242567155929064</volumetric_flow>
            <molar_enthalpy>-59.1906063717268</molar_enthalpy>
            <molar_entropy>-0.128215063434929</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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <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>Ethylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 3</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <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>Ethylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Aqueous</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
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              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Solid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Reactors.Reactor_Conversion</Type>
      <ReactorOperationMode>Isothermic</ReactorOperationMode>
      <ReactionSetID>DefaultSet</ReactionSetID>
      <ReactionSetName></ReactionSetName>
      <DeltaT>0</DeltaT>
      <DeltaQ>136.358948123781</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-95111686-a439-4407-be2c-7076c1345617</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-95111686-a439-4407-be2c-7076c1345617</Nome>
      <ShowQuickTable>false</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
      <ReactionSequence>
        <Item Index="0">aca6db79-2fde-4a6b-9c36-4436a394a088</Item>
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      <Reactions />
      <ReactionConversions>
        <Reaction ID="aca6db79-2fde-4a6b-9c36-4436a394a088">1</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_Fractions</CompositionBasis>
      <ComponentDescription>MAT-c63662d9-bd5b-4af9-b707-4fc66f86f6ff</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-c63662d9-bd5b-4af9-b707-4fc66f86f6ff</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-385a746d-d3b1-4e06-9402-5f054f64d7d2</PropertyPackage>
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            <Compound>
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              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
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              <MassFlow>0</MassFlow>
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              <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>
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              <Kvalue>NaN</Kvalue>
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              <FracaoMolar>0.5</FracaoMolar>
              <FracaoMassica>0.93296015813831</FracaoMassica>
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              <MassFlow>0.028054111955219</MassFlow>
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              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Kvalue>NaN</Kvalue>
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              <FracaoMolar>0.5</FracaoMolar>
              <FracaoMassica>0.0670398418616902</FracaoMassica>
              <MolarFlow>1.00000399070432</MolarFlow>
              <MassFlow>0.00201588804478102</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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            <enthalpy>-1.00573603560996</enthalpy>
            <entropy>1.52971636865177</entropy>
            <molarflow>2.00000798140864</molarflow>
            <massflow>0.03007</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>2.39049332365075</heatCapacityCp>
            <heatCapacityCv>1.83104770469999</heatCapacityCv>
            <molecularWeight>15.03494</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.0991978726586119</thermalConductivity>
            <volumetric_flow>0.0488378811744866</volumetric_flow>
            <molar_enthalpy>-15.1211809512336</molar_enthalpy>
            <molar_entropy>22.9991938196972</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>NaN</surfaceTension>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>1</ID>
          <Compounds>
            <Compound>
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              <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>
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              <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>Ethylene</Nome>
            </Compound>
            <Compound>
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              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>2</ID>
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            <Compound>
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              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
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              <MassFlow>0</MassFlow>
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              <ActivityCoeff>0.0240023448351224</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
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              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.5</FracaoMolar>
              <FracaoMassica>0.93296015813831</FracaoMassica>
              <MolarFlow>1.00000399070432</MolarFlow>
              <MassFlow>0.028054111955219</MassFlow>
              <FugacityCoeff>0.994757642112892</FugacityCoeff>
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              <PartialVolume>0.0243354900614989</PartialVolume>
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              <Descricao></Descricao>
              <Nome>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.5</FracaoMolar>
              <FracaoMassica>0.0670398418616902</FracaoMassica>
              <MolarFlow>1.00000399070432</MolarFlow>
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              <FugacityCoeff>1.00155816525887</FugacityCoeff>
              <ActivityCoeff>4.3229793519444E-16</ActivityCoeff>
              <PartialVolume>0.0245021937970947</PartialVolume>
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              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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            <enthalpy>-1.00573603560996</enthalpy>
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            <massflow>0.03007</massflow>
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            <massfraction>1</massfraction>
            <heatCapacityCp>2.39049332365075</heatCapacityCp>
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            <viscosity>9.75628267856151E-06</viscosity>
            <kinematic_viscosity>1.58455661509907E-05</kinematic_viscosity>
            <volumetric_flow>0.0488378811744866</volumetric_flow>
            <molar_enthalpy>-15.1211809512336</molar_enthalpy>
            <molar_entropy>22.9991938196972</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
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              <MassFlow>0</MassFlow>
              <FugacityCoeff>40.7068796739991</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
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              <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>0.589337048688285</FracaoMolar>
              <FracaoMassica>0.952315993171632</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>44.0517112291991</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.410662951311715</FracaoMolar>
              <FracaoMassica>0.0476840068283679</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>63.6699556840464</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <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>Ethylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 3</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <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>Ethylene</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>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Aqueous</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>7</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Solid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-d73dfa83-dbf4-4217-a512-338ebfb6f258</ComponentDescription>
      <ComponentName>liq</ComponentName>
      <code>0</code>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>CorrentedeMatria</Descricao>
      <Nome>MAT-d73dfa83-dbf4-4217-a512-338ebfb6f258</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-385a746d-d3b1-4e06-9402-5f054f64d7d2</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>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethane</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.589337048688285</FracaoMolar>
              <FracaoMassica>0.952315993171632</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.410662951311715</FracaoMolar>
              <FracaoMassica>0.0476840068283679</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>NaN</density>
            <enthalpy>NaN</enthalpy>
            <entropy>NaN</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>NaN</heatCapacityCp>
            <heatCapacityCv>NaN</heatCapacityCv>
            <molecularWeight>17.3611087941914</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.0851262540145728</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>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>NaN</FracaoMolar>
              <FracaoMassica>NaN</FracaoMassica>
              <MolarFlow>NaN</MolarFlow>
              <MassFlow>NaN</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>NaN</density>
            <enthalpy>0</enthalpy>
            <entropy>0</entropy>
            <molarflow>0</molarflow>
            <massflow>0</massflow>
            <molarfraction>0</molarfraction>
            <massfraction>0</massfraction>
            <heatCapacityCp>0</heatCapacityCp>
            <heatCapacityCv>0</heatCapacityCv>
            <molecularWeight>NaN</molecularWeight>
            <thermalConductivity>0</thermalConductivity>
            <viscosity>0</viscosity>
            <kinematic_viscosity>NaN</kinematic_viscosity>
            <volumetric_flow>NaN</volumetric_flow>
            <molar_enthalpy>NaN</molar_enthalpy>
            <molar_entropy>NaN</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>2</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.993103518171863</FugacityCoeff>
              <ActivityCoeff>0.0239906278311139</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>0.589337048688285</FracaoMolar>
              <FracaoMassica>0.952315993171632</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.994343234290249</FugacityCoeff>
              <ActivityCoeff>0.0143282986163199</ActivityCoeff>
              <PartialVolume>0.0243252471811943</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Ethylene</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.410662951311715</FracaoMolar>
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              <Descricao></Descricao>
              <Nome>Hydrogen</Nome>
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          <Descricao></Descricao>
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            <molar_entropy>27.7277438087203</molar_entropy>
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          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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        </Phase>
        <Phase>
          <ID>3</ID>
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              <Kvalue>0</Kvalue>
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              <VolumetricFraction>0</VolumetricFraction>
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              <Nome>Ethane</Nome>
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              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <VolumetricFraction>0</VolumetricFraction>
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              <Nome>Ethylene</Nome>
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              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
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              <Nome>Hydrogen</Nome>
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          <Nome>Liquid 1</Nome>
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          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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              <Nome>Ethylene</Nome>
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              <Nome>Hydrogen</Nome>
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          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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              <Nome>Ethylene</Nome>
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              <Nome>Hydrogen</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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              <Nome>Ethylene</Nome>
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          <TPMProperties>
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              <Nome>Ethylene</Nome>
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      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="RC-95111686-a439-4407-be2c-7076c1345617" 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>5143</X>
      <Y>3693</Y>
      <Name>EN-337997af-9d79-4805-a038-4386d09eedea</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="RC-95111686-a439-4407-be2c-7076c1345617" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
  </GraphicObjects>
  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-385a746d-d3b1-4e06-9402-5f054f64d7d2</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,Ethylene,Hydrogen</TPCompIDs>
      <Parameters>
        <Parameter ID="PP_PHFILT" Value="0.001" />
        <Parameter ID="PP_PSFILT" Value="0.001" />
        <Parameter ID="PP_PHFELT" Value="0.001" />
        <Parameter ID="PP_PSFELT" Value="0.001" />
        <Parameter ID="PP_PHFMEI" Value="50" />
        <Parameter ID="PP_PSFMEI" Value="50" />
        <Parameter ID="PP_PHFMII" Value="100" />
        <Parameter ID="PP_PSFMII" Value="100" />
        <Parameter ID="PP_PTFMEI" Value="100" />
        <Parameter ID="PP_PTFMII" Value="100" />
        <Parameter ID="PP_PTFILT" Value="0.001" />
        <Parameter ID="PP_PTFELT" Value="0.001" />
        <Parameter ID="PP_FLASHALGORITHM" Value="2" />
        <Parameter ID="PP_IDEAL_MIXRULE_LIQDENS" Value="0" />
        <Parameter ID="PP_USEEXPLIQDENS" Value="0" />
        <Parameter ID="PP_USE_EOS_LIQDENS" Value="0" />
        <Parameter ID="PP_USE_EOS_VOLUME_SHIFT" Value="0" />
      </Parameters>
      <InteractionParameters>
        <InteractionParameter Compound1="Hydrogen" Compound2="Ethylene" Value="0.0633" />
        <InteractionParameter Compound1="Hydrogen" Compound2="Ethane" Value="-0.0756" />
        <InteractionParameter Compound1="Ethylene" Compound2="Ethane" Value="0.0119" />
      </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>Ethylene</Name>
      <CAS_Number>74-85-1</CAS_Number>
      <Formula>CH2CH2</Formula>
      <SMILES>C=C</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>28.054</Molar_Weight>
      <Critical_Temperature>282.34</Critical_Temperature>
      <Critical_Pressure>5041000</Critical_Pressure>
      <Critical_Volume>0.1311</Critical_Volume>
      <Critical_Compressibility>0.282</Critical_Compressibility>
      <Acentric_Factor>0.087</Acentric_Factor>
      <Z_Rackett>0.281</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.0949</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.00297044171744</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>61</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>7.81350253083339</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>1871.74734440721</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>2439.58080844086</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>62.154</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-2654.8</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-6.9413</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>2.3229E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>104</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>282.35</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>33071.93</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-860.0281</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>12.22807</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.000509703</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.628387E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-8.9556</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>288.21</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-0.21985</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-1.0831E-05</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>2.3782</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.29542</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>282.36</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.32456</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>103.18</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>282.35</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>68016</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-22414</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>286.75</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-1.1802</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.0017304</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>99.82</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>259.95</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.19499</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-11.178</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-0.31182</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>-0.0034844</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>3.5873E-07</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>100</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>280</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>9.3247E-06</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>1.4607</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>410.48</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-44405</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>170</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>590.92</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>2.1134E-06</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.41436</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>359.51</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>-2291.7</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>169.41</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>29.172</Solid_Density_Const_A>
      <Solid_Density_Const_B>-0.027595</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>73.15</Solid_Density_Tmin>
      <Solid_Density_Tmax>104</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.002859</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>236.18</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-7.9878</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0.032145</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-9.7469E-05</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>104</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>272.95</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>4815.2</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-937.58</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>68.923</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-1.0511</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0.0052386</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>10</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>103.97</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>169.42</Normal_Boiling_Point>
      <ID>201</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>21658000</HVap_A>
      <HVap_B>1.2164</HVap_B>
      <HVap_C>-2.1538</HVap_C>
      <HVap_D>2.0768</HVap_D>
      <HVap_TMIN>104</HVap_TMIN>
      <HVap_TMAX>282.35</HVap_TMAX>
      <UNIQUAC_R>1.57</UNIQUAC_R>
      <UNIQUAC_Q>1.49</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>104</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>3.351</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="CH2" Value="2" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH2" Value="2" />
      </MODFACGroups>
      <Elements />
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Hydrogen</Name>
      <CAS_Number>1333-74-0</CAS_Number>
      <Formula>H2</Formula>
      <SMILES>[H][H]</SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>2.01588</Molar_Weight>
      <Critical_Temperature>33.19</Critical_Temperature>
      <Critical_Pressure>1313000</Critical_Pressure>
      <Critical_Volume>0.064147</Critical_Volume>
      <Critical_Compressibility>0.305</Critical_Compressibility>
      <Acentric_Factor>-0.215993</Acentric_Factor>
      <Z_Rackett>0.3139</Z_Rackett>
      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0.00158781835225</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>31</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>64.7712165406671</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>0</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>0</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>13.05</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-97.534</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>1.0355</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>0.00031816</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>13.08</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>33.19</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>3994.325</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-48.69006</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>10.36209</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-0.000340144</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.960333E-07</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-32.531</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>97.304</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>5.9178</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-0.0031563</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>2.9613</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0.25981</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>33.19</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0.19104</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>13.84</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>33.18</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>14510</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>-1191.1</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>156.51</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>-6.1773</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0.087907</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>13.84</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>32</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>-0.34238</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>-4.3002</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>-0.53814</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0.0011639</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>-0.00021792</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>13.84</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>31</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0.0026851</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0.74366</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>13.289</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>-31.305</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>10</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>1600</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>1.7916E-07</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0.68557</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>-0.51413</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>132.61</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>13.95</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>2000</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>-0.003232</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>1.9865</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>-5.0915</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>-0.00046122</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>-0.00062971</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>13.95</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>32.18</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>5730</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>-1.3847E-11</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>1.1605E-12</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>-1.2321E-13</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>4.114E-15</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>13.95</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>23.45</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>20.39</Normal_Boiling_Point>
      <ID>902</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>1534700</HVap_A>
      <HVap_B>3.214</HVap_B>
      <HVap_C>-8.4567</HVap_C>
      <HVap_D>8.4646</HVap_D>
      <HVap_TMIN>13.95</HVap_TMIN>
      <HVap_TMAX>32.62</HVap_TMAX>
      <UNIQUAC_R>0.4092</UNIQUAC_R>
      <UNIQUAC_Q>0.5516</UNIQUAC_Q>
      <IsFPROPSSupported>true</IsFPROPSSupported>
      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation>101</VaporPressureEquation>
      <IdealgasCpEquation>16</IdealgasCpEquation>
      <LiquidViscosityEquation>101</LiquidViscosityEquation>
      <VaporViscosityEquation>102</VaporViscosityEquation>
      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
      <LiquidDensityEquation>105</LiquidDensityEquation>
      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
      <SurfaceTensionEquation>16</SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>ChemSep</OriginalDB>
      <CurrentDB>ChemSep</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName></COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>13.95</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0.1171</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups />
      <MODFACGroups />
      <Elements />
    </Compound>
  </Compounds>
  <ReactionSets>
    <ReactionSet>
      <ID>DefaultSet</ID>
      <Name>Default Set</Name>
      <Description>Default Reaction Set</Description>
      <Reactions>
        <Reaction Key="aca6db79-2fde-4a6b-9c36-4436a394a088" ReactionID="aca6db79-2fde-4a6b-9c36-4436a394a088" Rank="0" IsActive="true" />
      </Reactions>
    </ReactionSet>
  </ReactionSets>
  <Reactions>
    <Reaction>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Reaction</Type>
      <StoichBalance>0</StoichBalance>
      <ReactionHeatCO>0</ReactionHeatCO>
      <ReactionHeat>136330</ReactionHeat>
      <Equation>CH3CH3 --&gt; CH2CH2 + H2 </Equation>
      <Name></Name>
      <ID>aca6db79-2fde-4a6b-9c36-4436a394a088</ID>
      <Description></Description>
      <BaseReactant>Ethane</BaseReactant>
      <ReactionPhase>Vapor</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>100</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="Ethylene" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Hydrogen" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
      </Compounds>
    </Reaction>
  </Reactions>
  <OptimizationCases />
  <SensitivityAnalysis />
  <PetroleumAssays />
  <WatchItems />
  <Spreadsheet>
    <Data1></Data1>
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