<?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>2014-12-13T17:46:32.7334634+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>VAIO\tanmay.lad00</SimAutor>
    <SimComentario>simulation_details</SimComentario>
    <FilePath>H:\ex9.6.1.dwxml</FilePath>
    <BackupFileName>46108240.dwbcs</BackupFileName>
    <CalculatorActivated>true</CalculatorActivated>
    <PropertyPackageFlashAlgorithm>DWSIMDefault</PropertyPackageFlashAlgorithm>
    <PropertyPackageIOFlashQuickMode>true</PropertyPackageIOFlashQuickMode>
    <ThreePhaseFlashStabTestSeverity>0</ThreePhaseFlashStabTestSeverity>
    <FlashValidationDGETolerancePct>0.01</FlashValidationDGETolerancePct>
    <Password></Password>
    <UsePassword>false</UsePassword>
    <ThreePhaseFlashStabTestCompIds>Metano,Etano,Oxigenio,DioxidoDeCarbono,Agua</ThreePhaseFlashStabTestCompIds>
  </Settings>
  <SimulationObjects>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Methane (C1)</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-392b3af2-7784-4fc9-921d-9dbb65b01e6c</ComponentDescription>
      <ComponentName>NG + O2</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-392b3af2-7784-4fc9-921d-9dbb65b01e6c</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems>
        <NodeItem ID="2007626413" Checked="true" Text="PROP_MS_105,Oxigenio" Value="0.1759945" Unit="kg/s" />
      </NodeItems>
      <PropertyPackage>PP-cf8f8a63-9f3b-4868-b054-9dfdecdf8d65</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.130769230769231</FracaoMolar>
              <FracaoMassica>0.070240244811067</FracaoMassica>
              <MolarFlow>0.850000000000002</MolarFlow>
              <MassFlow>0.01363655</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0230769230769231</FracaoMolar>
              <FracaoMassica>0.0232330482578304</FracaoMassica>
              <MolarFlow>0.15</MolarFlow>
              <MassFlow>0.00451049999999999</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.846153846153846</FracaoMolar>
              <FracaoMassica>0.906526706931103</FracaoMassica>
              <MolarFlow>5.5</MolarFlow>
              <MassFlow>0.1759945</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>NaN</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</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>DioxidoDeCarbono</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>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>1.22233089501035</density>
            <enthalpy>-0.377506341059842</enthalpy>
            <entropy>0.197699839033716</entropy>
            <molarflow>6.5</molarflow>
            <massflow>0.19414155</massflow>
            <heatCapacityCp>1.03601353032407</heatCapacityCp>
            <heatCapacityCv>0.755375024253041</heatCapacityCv>
            <molecularWeight>29.8679307692308</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.0282696894721906</thermalConductivity>
            <volumetric_flow>0.158828964229327</volumetric_flow>
            <molar_enthalpy>-11.275333259721</molar_enthalpy>
            <molar_entropy>5.90488510534708</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>Metano</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>Etano</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>Oxigenio</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>DioxidoDeCarbono</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>1.72948957531868E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>NaN</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</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>0.130769230769231</FracaoMolar>
              <FracaoMassica>0.0702402448110671</FracaoMassica>
              <MolarFlow>0.850000000000001</MolarFlow>
              <MassFlow>0.01363655</MassFlow>
              <FugacityCoeff>0.997912103825654</FugacityCoeff>
              <ActivityCoeff>0.001670043412766</ActivityCoeff>
              <PartialVolume>0.0244129589440715</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.0207510160807309</VolumetricFlow>
              <VolumetricFraction>0.130650074949612</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0230769230769231</FracaoMolar>
              <FracaoMassica>0.0232330482578305</FracaoMassica>
              <MolarFlow>0.15</MolarFlow>
              <MassFlow>0.00451050000000001</MassFlow>
              <FugacityCoeff>0.994622680940134</FugacityCoeff>
              <ActivityCoeff>0.0240950795501209</ActivityCoeff>
              <PartialVolume>0.0243322124895125</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.00364983204549177</VolumetricFlow>
              <VolumetricFraction>0.0229796376448184</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.846153846153846</FracaoMolar>
              <FracaoMassica>0.906526706931102</FracaoMassica>
              <MolarFlow>5.5</MolarFlow>
              <MassFlow>0.1759945</MassFlow>
              <FugacityCoeff>0.99907665242669</FugacityCoeff>
              <ActivityCoeff>0.000556973259846219</ActivityCoeff>
              <PartialVolume>0.0244414745028597</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.134428116103105</VolumetricFlow>
              <VolumetricFraction>0.84637028740557</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</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>0.995926341240556</FugacityCoeff>
              <ActivityCoeff>0.0156504264639077</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</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>0.991326837418684</FugacityCoeff>
              <ActivityCoeff>31.6694059861062</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.998822060102149</compressibilityFactor>
            <density>1.22233089501035</density>
            <enthalpy>-0.377506341059842</enthalpy>
            <entropy>0.197699839033716</entropy>
            <molarflow>6.5</molarflow>
            <massflow>0.19414155</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>1.03601353032407</heatCapacityCp>
            <heatCapacityCv>0.755375024253041</heatCapacityCv>
            <molecularWeight>29.8679307692308</molecularWeight>
            <thermalConductivity>0.0282696894721906</thermalConductivity>
            <viscosity>1.92535783775765E-05</viscosity>
            <kinematic_viscosity>1.57515272306142E-05</kinematic_viscosity>
            <volumetric_flow>0.158828964229327</volumetric_flow>
            <molar_enthalpy>-11.275333259721</molar_enthalpy>
            <molar_entropy>5.90488510534708</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>3</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Nome>DioxidoDeCarbono</Nome>
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          <Descricao></Descricao>
          <Nome>Aqueous</Nome>
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              <Nome>DioxidoDeCarbono</Nome>
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          <Descricao></Descricao>
          <Nome>Solid</Nome>
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      <CompoundConversions />
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      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-92033af2-67d7-4aad-8d23-5b8c5b864452</ComponentDescription>
      <ComponentName>vapor</ComponentName>
      <code>0</code>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
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              <Nome>DioxidoDeCarbono</Nome>
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              <Nome>Oxigenio</Nome>
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              <Nome>DioxidoDeCarbono</Nome>
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              <Nome>DioxidoDeCarbono</Nome>
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              <Nome>Agua</Nome>
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          <Nome>Liquid 1</Nome>
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              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</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>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</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>DioxidoDeCarbono</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>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>5</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 3</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>6</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</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>Metano</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>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</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>DioxidoDeCarbono</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>Agua</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>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-27cb0daf-01ab-44f8-a128-8ced6aceb8e2</ComponentDescription>
      <ComponentName>water</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-27cb0daf-01ab-44f8-a128-8ced6aceb8e2</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-cf8f8a63-9f3b-4868-b054-9dfdecdf8d65</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
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            <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>
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              <PartialVolume>0</PartialVolume>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>NaN</lnKvalue>
              <Kvalue>NaN</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>12.8873261786661</lnKvalue>
              <Kvalue>395270.720968811</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>1.82231187954952E-06</FracaoMolar>
              <FracaoMassica>3.23676522317062E-06</FracaoMassica>
              <MolarFlow>3.69776051974873E-06</MolarFlow>
              <MassFlow>1.1832463887144E-07</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>9.40662771911866</lnKvalue>
              <Kvalue>12168.7652109245</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>2.0797018192412E-05</FracaoMolar>
              <FracaoMassica>5.08047743535422E-05</FracaoMassica>
              <MolarFlow>4.220045627942E-05</MolarFlow>
              <MassFlow>1.85724208085728E-06</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.999977380669928</FracaoMolar>
              <FracaoMassica>0.999945958460423</FracaoMassica>
              <MolarFlow>2.02911308452705</MolarFlow>
              <MassFlow>0.0365544722177548</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>1041.66527259381</density>
            <enthalpy>-2539.23090844779</enthalpy>
            <entropy>-6.83815812540182</entropy>
            <molarflow>2.02915898274385</molarflow>
            <massflow>0.0365564477844745</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>0.188297908327581</massfraction>
            <heatCapacityCp>3.92715186672121</heatCapacityCp>
            <heatCapacityCv>3.04841384804638</heatCapacityCv>
            <molecularWeight>18.0155661016972</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.30705997771987</thermalConductivity>
            <volumetric_flow>3.50942368400616E-05</volumetric_flow>
            <molar_enthalpy>-45745.6822786138</molar_enthalpy>
            <molar_entropy>-123.193289722035</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>0.106492447478476</surfaceTension>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>1</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>1.82231187954952E-06</FracaoMolar>
              <FracaoMassica>3.23676522317062E-06</FracaoMassica>
              <MolarFlow>3.69776051974873E-06</MolarFlow>
              <MassFlow>1.1832463887144E-07</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>2.0797018192412E-05</FracaoMolar>
              <FracaoMassica>5.08047743535422E-05</FracaoMassica>
              <MolarFlow>4.220045627942E-05</MolarFlow>
              <MassFlow>1.85724208085728E-06</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.999977380669928</FracaoMolar>
              <FracaoMassica>0.999945958460423</FracaoMassica>
              <MolarFlow>2.02911308452705</MolarFlow>
              <MassFlow>0.0365544722177548</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>1.72948957531868E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0</compressibilityFactor>
            <density>1041.66527259381</density>
            <enthalpy>-2539.23090844779</enthalpy>
            <entropy>-6.83815812540182</entropy>
            <molarflow>2.02915898274385</molarflow>
            <massflow>0.0365564477844745</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.92715186672121</heatCapacityCp>
            <heatCapacityCv>3.04841384804638</heatCapacityCv>
            <molecularWeight>18.0155661016972</molecularWeight>
            <thermalConductivity>0.30705997771987</thermalConductivity>
            <viscosity>0.000912511435506148</viscosity>
            <kinematic_viscosity>8.76012150461671E-07</kinematic_viscosity>
            <volumetric_flow>0</volumetric_flow>
            <molar_enthalpy>-45745.6822786138</molar_enthalpy>
            <molar_entropy>-123.193289722035</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>0.997956870292946</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
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              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</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>0.994275910234197</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.720306530459568</FracaoMolar>
              <FracaoMassica>0.664882174127278</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.99921610433848</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.253074031470787</FracaoMolar>
              <FracaoMassica>0.321284580494636</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.995216750862775</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.026619438069645</FracaoMolar>
              <FracaoMassica>0.0138332453780854</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.989988016169321</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Vapor</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>3</ID>
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            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Kvalue>0</Kvalue>
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              <MassFlow>0</MassFlow>
              <FugacityCoeff>1083625.61931642</FugacityCoeff>
              <ActivityCoeff>1813.48820252415</ActivityCoeff>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
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              <lnKvalue>0</lnKvalue>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
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              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>1004764.19044185</FugacityCoeff>
              <ActivityCoeff>24340.7611366007</ActivityCoeff>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>1.82231187954952E-06</FracaoMolar>
              <FracaoMassica>3.23676522317062E-06</FracaoMassica>
              <MolarFlow>3.69776051974873E-06</MolarFlow>
              <MassFlow>1.1832463887144E-07</MassFlow>
              <FugacityCoeff>395028.186828434</FugacityCoeff>
              <ActivityCoeff>220.223479764601</ActivityCoeff>
              <PartialVolume>NaN</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>2.0797018192412E-05</FracaoMolar>
              <FracaoMassica>5.08047743535422E-05</FracaoMassica>
              <MolarFlow>4.220045627942E-05</MolarFlow>
              <MassFlow>1.85724208085728E-06</MassFlow>
              <FugacityCoeff>12105.3907996356</FugacityCoeff>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
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              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.999977380669928</FracaoMolar>
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              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.000868095672533575</compressibilityFactor>
            <density>1041.66527259381</density>
            <enthalpy>-2539.23090844779</enthalpy>
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            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.92715186672121</heatCapacityCp>
            <heatCapacityCv>3.04841384804638</heatCapacityCv>
            <molecularWeight>18.0155661016972</molecularWeight>
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            <viscosity>0.000912511435506148</viscosity>
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            <volumetric_flow>3.50942368400616E-05</volumetric_flow>
            <molar_enthalpy>-45745.6822786138</molar_enthalpy>
            <molar_entropy>-123.193289722035</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
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            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
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              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
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              <lnKvalue>0</lnKvalue>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
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              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
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              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
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              <lnKvalue>0</lnKvalue>
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              <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>Oxigenio</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>DioxidoDeCarbono</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>Agua</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>
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            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</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>
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              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</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>
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              <Kvalue>0</Kvalue>
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              <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>Metano</Nome>
            </Compound>
            <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>Etano</Nome>
            </Compound>
            <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>Oxigenio</Nome>
            </Compound>
            <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>DioxidoDeCarbono</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>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Solid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.UnitOps.Heater</Type>
      <FixOnHeat>true</FixOnHeat>
      <Eficiencia>100</Eficiencia>
      <OutletVaporFraction>1</OutletVaporFraction>
      <OutletTemperature>298.15</OutletTemperature>
      <CalcMode>OutletVaporFraction</CalcMode>
      <DeltaP>0</DeltaP>
      <DeltaT>76.4736098747168</DeltaT>
      <DeltaQ>97.9564802016947</DeltaQ>
      <ScriptExt_FontName>Courier New</ScriptExt_FontName>
      <ScriptExt_FontSize>10</ScriptExt_FontSize>
      <ScriptExt_ScriptTextB></ScriptExt_ScriptTextB>
      <ScriptExt_ScriptTextA></ScriptExt_ScriptTextA>
      <ScriptExt_Language>IronPython</ScriptExt_Language>
      <ErrorMessage></ErrorMessage>
      <ComponentDescription>Aquecedor</ComponentDescription>
      <ComponentName>AQ-a6e752a1-ed97-4055-8e06-8087472dca7f</ComponentName>
      <ValStatus>CAPE_VALID</ValStatus>
      <code>0</code>
      <selectedReport></selectedReport>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>Aquecedor</Descricao>
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      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
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    <SimulationObject>
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      <CompositionBasis>Molar_Flows</CompositionBasis>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-40290322-612c-4875-8136-47d975f11394</ComponentDescription>
      <ComponentName>watervapor</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-40290322-612c-4875-8136-47d975f11394</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-cf8f8a63-9f3b-4868-b054-9dfdecdf8d65</PropertyPackage>
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              <Nome>Etano</Nome>
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              <Nome>Oxigenio</Nome>
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              <FracaoMolar>2.0797018192412E-05</FracaoMolar>
              <FracaoMassica>5.08047743535422E-05</FracaoMassica>
              <MolarFlow>4.220045627942E-05</MolarFlow>
              <MassFlow>1.85724208085728E-06</MassFlow>
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              <Nome>DioxidoDeCarbono</Nome>
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              <Nome>Agua</Nome>
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          <Descricao></Descricao>
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            <molar_entropy>-34.3265073744637</molar_entropy>
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          <TPMProperties>
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            <surfaceTension>0.0787103674620671</surfaceTension>
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              <ActivityCoeff>NaN</ActivityCoeff>
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              <Nome>Oxigenio</Nome>
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              <MassFlow>1.38842232466664E-10</MassFlow>
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              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
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              <PartialVolume>1.8779656713254E-05</PartialVolume>
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              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Overall Liquid</Nome>
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            <viscosity>0.00027505088219601</viscosity>
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            <molar_enthalpy>-39488.2295023179</molar_enthalpy>
            <molar_entropy>-104.426067446446</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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        </Phase>
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              <Nome>Metano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <FracaoMolar>2.91566263013832E-06</FracaoMolar>
              <FracaoMassica>5.17866212727229E-06</FracaoMassica>
              <MolarFlow>3.69771438537233E-06</MolarFlow>
              <MassFlow>1.18323162617529E-07</MassFlow>
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              <VolumetricFraction>2.95303702250751E-06</VolumetricFraction>
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              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
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              <FracaoMolar>3.32725738323495E-05</FracaoMolar>
              <FracaoMassica>8.12796203143861E-05</FracaoMassica>
              <MolarFlow>4.21970887943249E-05</MolarFlow>
              <MassFlow>1.85709387783824E-06</MassFlow>
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              <Nome>DioxidoDeCarbono</Nome>
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              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
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              <Nome>Agua</Nome>
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          <Nome>Vapor</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
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          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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              <Nome>Metano</Nome>
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              <Nome>Etano</Nome>
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              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
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              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
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              <Descricao></Descricao>
              <Nome>Agua</Nome>
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          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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              <Nome>Metano</Nome>
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              <Nome>Etano</Nome>
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              <PartialVolume>0</PartialVolume>
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              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
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              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
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              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
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              <Descricao></Descricao>
              <Nome>Agua</Nome>
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          <Descricao></Descricao>
          <Nome>Liquid 2</Nome>
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            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
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              <Nome>Metano</Nome>
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              <Descricao></Descricao>
              <Nome>Etano</Nome>
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              <lnKvalue>0</lnKvalue>
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              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
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              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
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              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
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              <PartialVolume>0</PartialVolume>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</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>
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              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metano</Nome>
            </Compound>
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              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
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              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>DioxidoDeCarbono</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</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>
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            <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>Metano</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>Etano</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Oxigenio</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>DioxidoDeCarbono</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>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Solid</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
      </Phases>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.EnergyStream</Type>
      <Energia>97.9564802016947</Energia>
      <ComponentDescription>EN-563f5e3d-2af2-4231-b69f-3e357ea757f1</ComponentDescription>
      <ComponentName>e2</ComponentName>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
      <Descricao>Correntedeenergia</Descricao>
      <Nome>EN-563f5e3d-2af2-4231-b69f-3e357ea757f1</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
    </SimulationObject>
  </SimulationObjects>
  <GraphicObjects>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>NG + O2</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5108</X>
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      <EnergyConnector>
        <Connector IsAttached="False" />
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      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.ReactorConversionGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
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      <EnergyConnector>
        <Connector IsAttached="False" />
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      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>WhiteSmoke</FillColor>
      <LineWidth>2</LineWidth>
      <Width>20</Width>
      <Height>20</Height>
      <Rotation>0</Rotation>
      <X>5287</X>
      <Y>3584</Y>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>CorrentedeMatria</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>MaterialStream</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>vapor</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <Name>MAT-92033af2-67d7-4aad-8d23-5b8c5b864452</Name>
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      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>WhiteSmoke</FillColor>
      <LineWidth>2</LineWidth>
      <Width>20</Width>
      <Height>20</Height>
      <Rotation>0</Rotation>
      <X>5289</X>
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      <Fill>true</Fill>
      <MixPoint>false</MixPoint>
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      <Description>CorrentedeMatria</Description>
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      <TipoObjeto>MaterialStream</TipoObjeto>
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      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>water</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
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      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="AQ-a6e752a1-ed97-4055-8e06-8087472dca7f" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
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      <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>
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      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Correntedeenergia</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
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      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>e1</Tag>
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      <IsConnector>false</IsConnector>
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      <EnergyConnector>
        <Connector IsAttached="False" />
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      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.HeaterGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
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      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Aquecedor</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>Heater</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>HEAT-000</Tag>
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      <IsConnector>false</IsConnector>
      <X>5377</X>
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      <EnergyConnector>
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      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>WhiteSmoke</FillColor>
      <LineWidth>2</LineWidth>
      <Width>20</Width>
      <Height>20</Height>
      <Rotation>0</Rotation>
      <X>5442</X>
      <Y>3642</Y>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
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      <Status>Calculated</Status>
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      <FlippedH>false</FlippedH>
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      <Active>true</Active>
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      <Tag>watervapor</Tag>
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      <EnergyConnector>
        <Connector IsAttached="False" />
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      <Type>Microsoft.MSDN.Samples.GraphicObjects.EnergyStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>LightYellow</FillColor>
      <LineWidth>2</LineWidth>
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      <Height>20</Height>
      <Rotation>0</Rotation>
      <X>5357</X>
      <Y>3687</Y>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <MixPoint>false</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Correntedeenergia</Description>
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      <FlippedV>false</FlippedV>
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      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>e2</Tag>
      <AutoSize>false</AutoSize>
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      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
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      <SpecialConnectors />
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  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-cf8f8a63-9f3b-4868-b054-9dfdecdf8d65</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>Metano,Etano,Oxigenio,DioxidoDeCarbono,Agua</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="Metano" Compound2="Etano" Value="-0.0033" />
        <InteractionParameter Compound1="Metano" Compound2="DioxidoDeCarbono" Value="0.0793" />
        <InteractionParameter Compound1="DioxidoDeCarbono" Compound2="Etano" Value="0.1326" />
        <InteractionParameter Compound1="DioxidoDeCarbono" Compound2="Agua" Value="0.0063" />
      </InteractionParameters>
    </PropertyPackage>
  </PropertyPackages>
  <Compounds>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Metano</Name>
      <CAS_Number>74-82-8</CAS_Number>
      <Formula>CH4</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>16.043</Molar_Weight>
      <Critical_Temperature>190.564</Critical_Temperature>
      <Critical_Pressure>4599000</Critical_Pressure>
      <Critical_Volume>0.0986</Critical_Volume>
      <Critical_Compressibility>0.286</Critical_Compressibility>
      <Acentric_Factor>0.01155</Acentric_Factor>
      <Z_Rackett>0.289</Z_Rackett>
      <PR_Volume_Translation_Coefficient>-0.1595</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0.0234</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>5.68</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>52</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>2.58324</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-4645.1</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-3147.21</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>39.205</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-1324.4</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-3.44</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>3.1E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>90.64</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>190.56</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>36.2</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-0.0511</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>0.000221</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-1.82E-07</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>4.89E-11</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-61.572</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>178.15</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-0.95239</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-9.06E-24</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>10</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>111.66</Normal_Boiling_Point>
      <ID>1</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>10194000</HVap_A>
      <HVap_B>0.26087</HVap_B>
      <HVap_C>-0.14694</HVap_C>
      <HVap_D>0.22154</HVap_D>
      <HVap_TMIN>90</HVap_TMIN>
      <HVap_TMAX>190</HVap_TMAX>
      <UNIQUAC_R>1.1239</UNIQUAC_R>
      <UNIQUAC_Q>1.152</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName>METHANE</COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="CH4" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH4" Value="1" />
      </MODFACGroups>
      <Elements>
        <Item Name="C" Value="1" />
        <Item Name="H" Value="4" />
      </Elements>
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Etano</Name>
      <CAS_Number>74-84-0</CAS_Number>
      <Formula>C2H6</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>30.07</Molar_Weight>
      <Critical_Temperature>305.32</Critical_Temperature>
      <Critical_Pressure>4872000</Critical_Pressure>
      <Critical_Volume>0.1455</Critical_Volume>
      <Critical_Compressibility>0.279</Critical_Compressibility>
      <Acentric_Factor>0.09949</Acentric_Factor>
      <Z_Rackett>0.281</Z_Rackett>
      <PR_Volume_Translation_Coefficient>-0.1134</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0.0605</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0.1064</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>6.05</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>68</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>3.1775</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-2787.5</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-1061.54</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>51.857</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-2598.7</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-5.1283</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>1.49E-05</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>90.35</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>305.32</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>33.3</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-0.0111</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>0.000357</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-3.76E-07</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.19E-10</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-70.046</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>276.38</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-0.6087</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-3.11E-18</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>7</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>184.55</Normal_Boiling_Point>
      <ID>2</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>21091000</HVap_A>
      <HVap_B>0.6046</HVap_B>
      <HVap_C>-0.55492</HVap_C>
      <HVap_D>0.32799</HVap_D>
      <HVap_TMIN>90</HVap_TMIN>
      <HVap_TMAX>305</HVap_TMAX>
      <UNIQUAC_R>1.8022</UNIQUAC_R>
      <UNIQUAC_Q>1.696</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName>ETHANE</COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="CH3" Value="2" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH3" Value="2" />
      </MODFACGroups>
      <Elements>
        <Item Name="C" Value="2" />
        <Item Name="H" Value="6" />
      </Elements>
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Oxigenio</Name>
      <CAS_Number>7782-44-7</CAS_Number>
      <Formula>O2</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>31.999</Molar_Weight>
      <Critical_Temperature>154.58</Critical_Temperature>
      <Critical_Pressure>5040000</Critical_Pressure>
      <Critical_Volume>0.0734</Critical_Volume>
      <Critical_Compressibility>0.288</Critical_Compressibility>
      <Acentric_Factor>0.0221798</Acentric_Factor>
      <Z_Rackett>0.29</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</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>0</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>0</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>51.245</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-1200.2</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-6.4361</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>0.028405</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>1</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>54</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>154</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>29.7</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-0.0099</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>3.99E-05</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-3.39E-08</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>9.18E-12</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-41.476</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>94.04</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-1.207</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>0</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>0</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>90.188</Normal_Boiling_Point>
      <ID>13</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>9008000</HVap_A>
      <HVap_B>0.4542</HVap_B>
      <HVap_C>-0.4096</HVap_C>
      <HVap_D>0.3183</HVap_D>
      <HVap_TMIN>54</HVap_TMIN>
      <HVap_TMAX>154</HVap_TMAX>
      <UNIQUAC_R>0.857</UNIQUAC_R>
      <UNIQUAC_Q>0.94</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName>OXYGEN</COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="O2" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="O2" Value="1" />
      </MODFACGroups>
      <Elements>
        <Item Name="O" Value="2" />
      </Elements>
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>DioxidoDeCarbono</Name>
      <CAS_Number>124-38-9</CAS_Number>
      <Formula>CO2</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>44.01</Molar_Weight>
      <Critical_Temperature>304.21</Critical_Temperature>
      <Critical_Pressure>7380000</Critical_Pressure>
      <Critical_Volume>0.094</Critical_Volume>
      <Critical_Compressibility>0.274</Critical_Compressibility>
      <Acentric_Factor>0.223621</Acentric_Factor>
      <Z_Rackett>0.272</Z_Rackett>
      <PR_Volume_Translation_Coefficient>-0.0817</PR_Volume_Translation_Coefficient>
      <SRK_Volume_Translation_Coefficient>0.0833</SRK_Volume_Translation_Coefficient>
      <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
      <Chao_Seader_Solubility_Parameter>0</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>0</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>2.69333</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-8941.4</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-8960.87</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>140.54</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-4735</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-21.268</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>0.040909</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>1</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>216.58</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>304.21</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>29.2</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-0.0224</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>0.000265</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-4.15E-07</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>2.01E-10</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>18.775</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>-402.92</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>-4.6854</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-6.92E-26</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>10</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>0</Normal_Boiling_Point>
      <ID>16</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>21730000</HVap_A>
      <HVap_B>0.382</HVap_B>
      <HVap_C>-0.4339</HVap_C>
      <HVap_D>0.42213</HVap_D>
      <HVap_TMIN>216.58</HVap_TMIN>
      <HVap_TMAX>304</HVap_TMAX>
      <UNIQUAC_R>1.2986</UNIQUAC_R>
      <UNIQUAC_Q>1.292</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName></COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="CO2" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CO2" Value="1" />
      </MODFACGroups>
      <Elements>
        <Item Name="C" Value="1" />
        <Item Name="O" Value="2" />
      </Elements>
    </Compound>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Agua</Name>
      <CAS_Number>7732-18-5</CAS_Number>
      <Formula>H2O</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>18.015</Molar_Weight>
      <Critical_Temperature>647.13</Critical_Temperature>
      <Critical_Pressure>22055000</Critical_Pressure>
      <Critical_Volume>0.0559</Critical_Volume>
      <Critical_Compressibility>0.229</Critical_Compressibility>
      <Acentric_Factor>0.34486</Acentric_Factor>
      <Z_Rackett>0.237</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</Chao_Seader_Solubility_Parameter>
      <Chao_Seader_Liquid_Molar_Volume>0</Chao_Seader_Liquid_Molar_Volume>
      <IG_Entropy_of_Formation_25C>2.61728</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-13422</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-12689</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>6.17E-30</Dipole_Moment>
      <Vapor_Pressure_Constant_A>73.649</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-7258.2</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-7.3037</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>4.17E-06</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>273.16</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>647.13</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>33.8</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>-0.00594</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>2.24E-05</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-9.96E-09</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>1.1E-12</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-52.843</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>3703.6</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>5.866</Liquid_Viscosity_Const_C>
      <Liquid_Viscosity_Const_D>-5.88E-29</Liquid_Viscosity_Const_D>
      <Liquid_Viscosity_Const_E>10</Liquid_Viscosity_Const_E>
      <Liquid_Density_Const_A>0</Liquid_Density_Const_A>
      <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
      <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
      <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
      <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
      <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
      <Liquid_Heat_Capacity_Const_A>0</Liquid_Heat_Capacity_Const_A>
      <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
      <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
      <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
      <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
      <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
      <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
      <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
      <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
      <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
      <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
      <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
      <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
      <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
      <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
      <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
      <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
      <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
      <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
      <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
      <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
      <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
      <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
      <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
      <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
      <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
      <Solid_Density_Const_A>0</Solid_Density_Const_A>
      <Solid_Density_Const_B>0</Solid_Density_Const_B>
      <Solid_Density_Const_C>0</Solid_Density_Const_C>
      <Solid_Density_Const_D>0</Solid_Density_Const_D>
      <Solid_Density_Const_E>0</Solid_Density_Const_E>
      <Solid_Density_Tmin>0</Solid_Density_Tmin>
      <Solid_Density_Tmax>0</Solid_Density_Tmax>
      <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
      <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
      <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
      <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
      <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
      <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
      <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
      <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
      <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
      <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
      <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
      <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
      <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
      <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
      <Normal_Boiling_Point>373.15</Normal_Boiling_Point>
      <ID>15</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>52053000</HVap_A>
      <HVap_B>0.3199</HVap_B>
      <HVap_C>-0.212</HVap_C>
      <HVap_D>0.25795</HVap_D>
      <HVap_TMIN>273</HVap_TMIN>
      <HVap_TMAX>647</HVap_TMAX>
      <UNIQUAC_R>0.92</UNIQUAC_R>
      <UNIQUAC_Q>1.4</UNIQUAC_Q>
      <IsFPROPSSupported>false</IsFPROPSSupported>
      <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
      <IsModified>false</IsModified>
      <VaporPressureEquation></VaporPressureEquation>
      <IdealgasCpEquation></IdealgasCpEquation>
      <LiquidViscosityEquation></LiquidViscosityEquation>
      <VaporViscosityEquation></VaporViscosityEquation>
      <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
      <LiquidDensityEquation></LiquidDensityEquation>
      <LiquidHeatCapacityEquation></LiquidHeatCapacityEquation>
      <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
      <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
      <SolidDensityEquation></SolidDensityEquation>
      <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
      <SurfaceTensionEquation></SurfaceTensionEquation>
      <PC_SAFT_sigma>0</PC_SAFT_sigma>
      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
      <PC_SAFT_m>0</PC_SAFT_m>
      <OriginalDB>DWSIM</OriginalDB>
      <CurrentDB>DWSIM</CurrentDB>
      <CompCreatorStudyFile></CompCreatorStudyFile>
      <COSMODBName>WATER</COSMODBName>
      <IsIon>false</IsIon>
      <IsSalt>false</IsSalt>
      <IsHydratedSalt>false</IsHydratedSalt>
      <HydrationNumber>0</HydrationNumber>
      <Charge>0</Charge>
      <PositiveIon></PositiveIon>
      <NegativeIon></NegativeIon>
      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
      <StoichSum>0</StoichSum>
      <Electrolyte_DelGF>0</Electrolyte_DelGF>
      <Electrolyte_DelHF>0</Electrolyte_DelHF>
      <Electrolyte_Cp0>0</Electrolyte_Cp0>
      <TemperatureOfFusion>0</TemperatureOfFusion>
      <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
      <SolidTs>0</SolidTs>
      <SolidDensityAtTs>0</SolidDensityAtTs>
      <StandardStateMolarVolume>0</StandardStateMolarVolume>
      <MolarVolume_v2i>0</MolarVolume_v2i>
      <MolarVolume_v3i>0</MolarVolume_v3i>
      <MolarVolume_k1i>0</MolarVolume_k1i>
      <MolarVolume_k2i>0</MolarVolume_k2i>
      <MolarVolume_k3i>0</MolarVolume_k3i>
      <Ion_CpAq_a>0</Ion_CpAq_a>
      <Ion_CpAq_b>0</Ion_CpAq_b>
      <Ion_CpAq_c>0</Ion_CpAq_c>
      <UNIFACGroups>
        <Item Name="H2O" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="H2O" Value="1" />
      </MODFACGroups>
      <Elements>
        <Item Name="H" Value="2" />
        <Item Name="O" Value="1" />
      </Elements>
    </Compound>
  </Compounds>
  <ReactionSets>
    <ReactionSet>
      <ID>DefaultSet</ID>
      <Name>Default Set</Name>
      <Description>Default Reaction Set</Description>
      <Reactions>
        <Reaction Key="00820789-5168-4df1-97cf-1f9bbaaed903" ReactionID="00820789-5168-4df1-97cf-1f9bbaaed903" Rank="0" IsActive="true" />
        <Reaction Key="43d180bc-329f-45fd-aaaa-803df06ce08d" ReactionID="43d180bc-329f-45fd-aaaa-803df06ce08d" Rank="0" IsActive="true" />
      </Reactions>
    </ReactionSet>
  </ReactionSets>
  <Reactions>
    <Reaction>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Reaction</Type>
      <StoichBalance>0</StoichBalance>
      <ReactionHeatCO>0</ReactionHeatCO>
      <ReactionHeat>-802584.3347</ReactionHeat>
      <Equation>CH4 + 2O2 --&gt; CO2 + 2H2O </Equation>
      <Name>combustion1</Name>
      <ID>00820789-5168-4df1-97cf-1f9bbaaed903</ID>
      <Description></Description>
      <BaseReactant>Metano</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="Metano" StoichCoeff="-1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="true" />
        <Compound Name="Oxigenio" StoichCoeff="-2" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="DioxidoDeCarbono" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Agua" StoichCoeff="2" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
      </Compounds>
    </Reaction>
    <Reaction>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Reaction</Type>
      <StoichBalance>0</StoichBalance>
      <ReactionHeatCO>0</ReactionHeatCO>
      <ReactionHeat>-1428593.893</ReactionHeat>
      <Equation>C2H6 + 3.5O2 --&gt; 2CO2 + 3H2O </Equation>
      <Name>combustion2</Name>
      <ID>43d180bc-329f-45fd-aaaa-803df06ce08d</ID>
      <Description></Description>
      <BaseReactant>Etano</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="Etano" StoichCoeff="-1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="true" />
        <Compound Name="Oxigenio" StoichCoeff="-3.5" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="DioxidoDeCarbono" StoichCoeff="2" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
        <Compound Name="Agua" StoichCoeff="3" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
      </Compounds>
    </Reaction>
  </Reactions>
  <OptimizationCases />
  <SensitivityAnalysis />
  <PetroleumAssays />
  <WatchItems />
  <Spreadsheet>
    <Data1></Data1>
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&lt;!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.--&gt;
&lt;!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!--&gt;
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