<?xml version="1.0" encoding="utf-8"?>
<DWSIM_Simulation_Data>
  <GeneralInfo>
    <BuildVersion>3.2.5398.28421</BuildVersion>
    <BuildDate>2014-10-12T15:47:22</BuildDate>
    <OSInfo>Microsoft Windows 8 Single Language, Version 6.2.9200.0, Win32NT Platform</OSInfo>
    <SavedOn>2014-12-10T13:52:35.0824442-08:00</SavedOn>
  </GeneralInfo>
  <Settings>
    <Type>DWSIM.DWSIM.FormClasses.ClsFormOptions</Type>
    <SimulationMode></SimulationMode>
    <SelectedUnitSystem>
      <Type>DWSIM.DWSIM.SistemasDeUnidades.UnidadesCGS</Type>
      <nome>CGS System</nome>
      <area>cm2</area>
      <distance>cm</distance>
      <time>s</time>
      <volume>cm3</volume>
      <molar_volume>cm3/mol</molar_volume>
      <diameter>mm</diameter>
      <thickness>cm</thickness>
      <molar_conc>mol/cm3</molar_conc>
      <mass_conc>g/cm3</mass_conc>
      <heat_transf_coeff>cal/[cm2.s.C]</heat_transf_coeff>
      <force>dyn</force>
      <accel>cm/s2</accel>
      <spec_vol>cm3/g</spec_vol>
      <reac_rate>mol.[cm3.s]</reac_rate>
      <velocity>cm/s</velocity>
      <foulingfactor>C.cm2.s/cal</foulingfactor>
      <cakeresistance>cm/g</cakeresistance>
      <mediumresistance>cm-1</mediumresistance>
      <molar_enthalpy>cal/mol</molar_enthalpy>
      <molar_entropy>cal/[mol.C]</molar_entropy>
      <tdp_idealGasHeatCapacity>cal/[g.C]</tdp_idealGasHeatCapacity>
      <tdp_surfaceTension>dyn/cm</tdp_surfaceTension>
      <tdp_thermalConductivityOfLiquid>cal/[cm.s.C]</tdp_thermalConductivityOfLiquid>
      <tdp_thermalConductivityOfVapor>cal/[cm.s.C]</tdp_thermalConductivityOfVapor>
      <tdp_vaporPressure>atm</tdp_vaporPressure>
      <tdp_viscosityOfLiquid>cP</tdp_viscosityOfLiquid>
      <tdp_viscosityOfVapor>cP</tdp_viscosityOfVapor>
      <pdp_boilingPointTemperature>C</pdp_boilingPointTemperature>
      <pdp_meltingTemperature>C</pdp_meltingTemperature>
      <spmp_activity>atm</spmp_activity>
      <spmp_activityCoefficient>-</spmp_activityCoefficient>
      <spmp_compressibility>atm-1</spmp_compressibility>
      <spmp_compressibilityFactor>-</spmp_compressibilityFactor>
      <spmp_density>g/cm3</spmp_density>
      <spmp_enthalpy>cal/g</spmp_enthalpy>
      <spmp_entropy>cal/[g.C]</spmp_entropy>
      <spmp_excessEnthalpy>cal/g</spmp_excessEnthalpy>
      <spmp_excessEntropy>cal/[g.C]</spmp_excessEntropy>
      <spmp_molarflow>mol/s</spmp_molarflow>
      <spmp_massflow>g/s</spmp_massflow>
      <spmp_molarfraction>-</spmp_molarfraction>
      <spmp_massfraction>-</spmp_massfraction>
      <spmp_fugacity>atm</spmp_fugacity>
      <spmp_fugacityCoefficient>-</spmp_fugacityCoefficient>
      <spmp_heatCapacityCp>cal/[g.C]</spmp_heatCapacityCp>
      <spmp_heatCapacityCv>cal/[g.C]</spmp_heatCapacityCv>
      <spmp_jouleThomsonCoefficient>C/atm</spmp_jouleThomsonCoefficient>
      <spmp_logFugacityCoefficient>-</spmp_logFugacityCoefficient>
      <spmp_molecularWeight>g/mol</spmp_molecularWeight>
      <spmp_pressure>atm</spmp_pressure>
      <spmp_temperature>C</spmp_temperature>
      <spmp_speedOfSound>cm/s</spmp_speedOfSound>
      <spmp_thermalConductivity>cal/[cm.s.C]</spmp_thermalConductivity>
      <spmp_viscosity>cP</spmp_viscosity>
      <spmp_cinematic_viscosity>cSt</spmp_cinematic_viscosity>
      <spmp_volumetricFlow>cm3/s</spmp_volumetricFlow>
      <spmp_heatflow>kcal/h</spmp_heatflow>
      <spmp_head>m</spmp_head>
      <spmp_deltaT>C.</spmp_deltaT>
      <spmp_deltaP>atm</spmp_deltaP>
      <tpmp_kvalue>-</tpmp_kvalue>
      <tpmp_logKvalue>-</tpmp_logKvalue>
      <tpmp_surfaceTension>dyn/cm2</tpmp_surfaceTension>
    </SelectedUnitSystem>
    <NumberFormat>#0.0####</NumberFormat>
    <FractionNumberFormat>#0.0######</FractionNumberFormat>
    <SempreCalcularFlashPH>false</SempreCalcularFlashPH>
    <CalculateBubbleAndDewPoints>false</CalculateBubbleAndDewPoints>
    <ValidateEquilibriumCalc>true</ValidateEquilibriumCalc>
    <UsePhaseIdentificationAlgorithm>true</UsePhaseIdentificationAlgorithm>
    <SimNome>simulation_title</SimNome>
    <SimAutor>DELL-PC\dell</SimAutor>
    <SimComentario>simulation_details</SimComentario>
    <FilePath>F:\dwsim423.dwxml</FilePath>
    <BackupFileName>69218998.dwbcs</BackupFileName>
    <CalculatorActivated>true</CalculatorActivated>
    <PropertyPackageFlashAlgorithm>DWSIMDefault</PropertyPackageFlashAlgorithm>
    <PropertyPackageIOFlashQuickMode>true</PropertyPackageIOFlashQuickMode>
    <ThreePhaseFlashStabTestSeverity>0</ThreePhaseFlashStabTestSeverity>
    <FlashValidationDGETolerancePct>0.01</FlashValidationDGETolerancePct>
    <Password></Password>
    <UsePassword>false</UsePassword>
    <ThreePhaseFlashStabTestCompIds>Metanol,Agua</ThreePhaseFlashStabTestCompIds>
  </Settings>
  <SimulationObjects>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent>Methanol (CH3OH)</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <CompositionBasis>Molar_Fractions</CompositionBasis>
      <ComponentDescription>MAT-5819667f-aaa3-477c-b5cf-9443823be855</ComponentDescription>
      <ComponentName>in1</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-5819667f-aaa3-477c-b5cf-9443823be855</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-82b71c26-d8f5-45ff-840f-c8b6b4b01ca2</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>1.1962282527387</lnKvalue>
              <Kvalue>3.30761786728283</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.272632343593934</FracaoMolar>
              <FracaoMassica>0.399999999999999</FracaoMassica>
              <MolarFlow>2.49672305099556</MolarFlow>
              <MassFlow>0.0799999999999999</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>8.13122654898588E-05</VolumetricFlow>
              <VolumetricFraction>0.461330635149053</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>-2.00205535878412</lnKvalue>
              <Kvalue>0.135057406339595</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.727367656406066</FracaoMolar>
              <FracaoMassica>0.6</FracaoMassica>
              <MolarFlow>6.66111573688593</MolarFlow>
              <MassFlow>0.12</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>9.49436761160728E-05</VolumetricFlow>
              <VolumetricFraction>0.538669364850947</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>1134.71352045059</density>
            <enthalpy>-1976.43531308015</enthalpy>
            <entropy>-5.37177538305592</entropy>
            <molarflow>9.1578387878815</molarflow>
            <massflow>0.2</massflow>
            <heatCapacityCp>3.5475637148132</heatCapacityCp>
            <heatCapacityCv>2.73890254259637</heatCapacityCv>
            <molecularWeight>21.8392138835921</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.24601017460375</thermalConductivity>
            <volumetric_flow>0.000176255941605932</volumetric_flow>
            <molar_enthalpy>-43163.7935294418</molar_enthalpy>
            <molar_entropy>-117.315351525173</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>0.0894686206999951</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>0.272632343593934</FracaoMolar>
              <FracaoMassica>0.399999999999999</FracaoMassica>
              <MolarFlow>2.49672305099556</MolarFlow>
              <MassFlow>0.0799999999999999</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>3.95170553747469E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.727367656406066</FracaoMolar>
              <FracaoMassica>0.6</FracaoMassica>
              <MolarFlow>6.66111573688593</MolarFlow>
              <MassFlow>0.12</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>1134.71352045059</density>
            <enthalpy>-1976.43531308015</enthalpy>
            <entropy>-5.37177538305592</entropy>
            <molarflow>9.1578387878815</molarflow>
            <massflow>0.2</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.5475637148132</heatCapacityCp>
            <heatCapacityCv>2.73890254259637</heatCapacityCv>
            <molecularWeight>21.8392138835921</molecularWeight>
            <thermalConductivity>0.24601017460375</thermalConductivity>
            <viscosity>0.000670757729971278</viscosity>
            <kinematic_viscosity>5.91125176427724E-07</kinematic_viscosity>
            <volumetric_flow>0</volumetric_flow>
            <molar_enthalpy>-43163.7935294418</molar_enthalpy>
            <molar_entropy>-117.315351525173</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>0.901763610870487</FracaoMolar>
              <FracaoMassica>0.942286513590437</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.974441743520705</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.0982363891295132</FracaoMolar>
              <FracaoMassica>0.0577134864095634</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.982947430586275</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>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.272632343593934</FracaoMolar>
              <FracaoMassica>0.399999999999999</FracaoMassica>
              <MolarFlow>2.49672305099556</MolarFlow>
              <MassFlow>0.0799999999999999</MassFlow>
              <FugacityCoeff>0.631111546689829</FugacityCoeff>
              <ActivityCoeff>3.4107342377484</ActivityCoeff>
              <PartialVolume>3.95170553747469E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>8.13122654898588E-05</VolumetricFlow>
              <VolumetricFraction>0.461330635149053</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.727367656406066</FracaoMolar>
              <FracaoMassica>0.6</FracaoMassica>
              <MolarFlow>6.66111573688593</MolarFlow>
              <MassFlow>0.12</MassFlow>
              <FugacityCoeff>0.0259945726423446</FugacityCoeff>
              <ActivityCoeff>0.830435173720662</ActivityCoeff>
              <PartialVolume>1.72948957531868E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>9.49436761160728E-05</VolumetricFlow>
              <VolumetricFraction>0.538669364850947</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.0011586177843249</compressibilityFactor>
            <density>1134.71352045059</density>
            <enthalpy>-1976.43531308015</enthalpy>
            <entropy>-5.37177538305592</entropy>
            <molarflow>9.1578387878815</molarflow>
            <massflow>0.2</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.5475637148132</heatCapacityCp>
            <heatCapacityCv>2.73890254259637</heatCapacityCv>
            <molecularWeight>21.8392138835921</molecularWeight>
            <thermalConductivity>0.24601017460375</thermalConductivity>
            <viscosity>0.000670757729971278</viscosity>
            <kinematic_viscosity>5.91125176427724E-07</kinematic_viscosity>
            <volumetric_flow>0.000176255941605932</volumetric_flow>
            <molar_enthalpy>-43163.7935294418</molar_enthalpy>
            <molar_entropy>-117.315351525173</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</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>Metanol</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>Metanol</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>Metanol</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>Methanol (CH3OH)</ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-21a3cd83-948c-47c2-9e09-68af35cbef68</ComponentDescription>
      <ComponentName>in2</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-21a3cd83-948c-47c2-9e09-68af35cbef68</Nome>
      <ShowQuickTable>true</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage>PP-82b71c26-d8f5-45ff-840f-c8b6b4b01ca2</PropertyPackage>
      <Phases>
        <Phase>
          <ID>0</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0.472184110999179</lnKvalue>
              <Kvalue>1.60349257717212</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.567450085721614</FracaoMolar>
              <FracaoMassica>0.7</FracaoMassica>
              <MolarFlow>3.27694900443168</MolarFlow>
              <MassFlow>0.105</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.000102373189249311</VolumetricFlow>
              <VolumetricFraction>0.749843164578615</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>-1.56879976574923</lnKvalue>
              <Kvalue>0.208295035221583</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.432549914278386</FracaoMolar>
              <FracaoMassica>0.3</FracaoMassica>
              <MolarFlow>2.49791840133222</MolarFlow>
              <MassFlow>0.045</MassFlow>
              <FugacityCoeff>0</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>3.41529459283577E-05</VolumetricFlow>
              <VolumetricFraction>0.250156835421385</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Mixture</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <density>1098.69073642785</density>
            <enthalpy>-1601.94112181457</enthalpy>
            <entropy>-4.39662281783771</entropy>
            <molarflow>5.77486740576391</molarflow>
            <massflow>0.15</massflow>
            <heatCapacityCp>3.24472707377302</heatCapacityCp>
            <heatCapacityCv>2.49653753410366</heatCapacityCv>
            <molecularWeight>25.9746223524171</molecularWeight>
            <pressure>101325</pressure>
            <temperature>298.15</temperature>
            <thermalConductivity>0.211955618586136</thermalConductivity>
            <volumetric_flow>0.000136526135177668</volumetric_flow>
            <molar_enthalpy>-41609.8156699409</molar_enthalpy>
            <molar_entropy>-114.200617319354</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
            <surfaceTension>0.0710571116962878</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>0.567450085721614</FracaoMolar>
              <FracaoMassica>0.7</FracaoMassica>
              <MolarFlow>3.27694900443168</MolarFlow>
              <MassFlow>0.105</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>NaN</ActivityCoeff>
              <PartialVolume>3.95170553747469E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
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              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.432549914278386</FracaoMolar>
              <FracaoMassica>0.3</FracaoMassica>
              <MolarFlow>2.49791840133222</MolarFlow>
              <MassFlow>0.045</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>1098.69073642785</density>
            <enthalpy>-1601.94112181457</enthalpy>
            <entropy>-4.39662281783771</entropy>
            <molarflow>5.77486740576391</molarflow>
            <massflow>0.15</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.24472707377302</heatCapacityCp>
            <heatCapacityCv>2.49653753410366</heatCapacityCv>
            <molecularWeight>25.9746223524171</molecularWeight>
            <thermalConductivity>0.211955618586136</thermalConductivity>
            <viscosity>0.00040931048816153</viscosity>
            <kinematic_viscosity>3.72543860242523E-07</kinematic_viscosity>
            <volumetric_flow>0</volumetric_flow>
            <molar_enthalpy>-41609.8156699409</molar_enthalpy>
            <molar_entropy>-114.200617319354</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>0.909902000370291</FracaoMolar>
              <FracaoMassica>0.9472641119992</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.974428627770519</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.090097999629709</FracaoMolar>
              <FracaoMassica>0.0527358880008002</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>0.982931812342751</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>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.567450085721614</FracaoMolar>
              <FracaoMassica>0.7</FracaoMassica>
              <MolarFlow>3.27694900443168</MolarFlow>
              <MassFlow>0.105</MassFlow>
              <FugacityCoeff>0.249616396144881</FugacityCoeff>
              <ActivityCoeff>1.34900905093587</ActivityCoeff>
              <PartialVolume>3.95170553747469E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0.000102373189249311</VolumetricFlow>
              <VolumetricFraction>0.749843164578615</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</Nome>
            </Compound>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0.432549914278386</FracaoMolar>
              <FracaoMassica>0.3</FracaoMassica>
              <MolarFlow>2.49791840133222</MolarFlow>
              <MassFlow>0.045</MassFlow>
              <FugacityCoeff>0.0327083249869271</FugacityCoeff>
              <ActivityCoeff>1.04491594904638</ActivityCoeff>
              <PartialVolume>1.72948957531868E-05</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>3.41529459283577E-05</VolumetricFlow>
              <VolumetricFraction>0.250156835421385</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Agua</Nome>
            </Compound>
          </Compounds>
          <Descricao></Descricao>
          <Nome>Liquid 1</Nome>
          <SPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.SinglePhaseMixtureProperties</Type>
            <compressibilityFactor>0.00147650356924086</compressibilityFactor>
            <density>1098.69073642785</density>
            <enthalpy>-1601.94112181457</enthalpy>
            <entropy>-4.39662281783771</entropy>
            <molarflow>5.77486740576391</molarflow>
            <massflow>0.15</massflow>
            <molarfraction>1</molarfraction>
            <massfraction>1</massfraction>
            <heatCapacityCp>3.24472707377302</heatCapacityCp>
            <heatCapacityCv>2.49653753410366</heatCapacityCv>
            <molecularWeight>25.9746223524171</molecularWeight>
            <thermalConductivity>0.211955618586136</thermalConductivity>
            <viscosity>0.00040931048816153</viscosity>
            <kinematic_viscosity>3.72543860242523E-07</kinematic_viscosity>
            <volumetric_flow>0.000136526135177668</volumetric_flow>
            <molar_enthalpy>-41609.8156699409</molar_enthalpy>
            <molar_entropy>-114.200617319354</molar_entropy>
          </SPMProperties>
          <TPMProperties>
            <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.TwoPhaseMixtureProperties</Type>
          </TPMProperties>
        </Phase>
        <Phase>
          <ID>4</ID>
          <Compounds>
            <Compound>
              <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.Substancia</Type>
              <lnKvalue>0</lnKvalue>
              <Kvalue>0</Kvalue>
              <FracaoDePetroleo>false</FracaoDePetroleo>
              <FracaoMolar>0</FracaoMolar>
              <FracaoMassica>0</FracaoMassica>
              <MolarFlow>0</MolarFlow>
              <MassFlow>0</MassFlow>
              <FugacityCoeff>NaN</FugacityCoeff>
              <ActivityCoeff>0</ActivityCoeff>
              <PartialVolume>0</PartialVolume>
              <PartialPressure>0</PartialPressure>
              <VolumetricFlow>0</VolumetricFlow>
              <VolumetricFraction>0</VolumetricFraction>
              <Descricao></Descricao>
              <Nome>Metanol</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>Metanol</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>Metanol</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>Metanol</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.UnitOps.Mixer</Type>
      <PressureCalculation>Minimum</PressureCalculation>
      <ScriptExt_FontName>Courier New</ScriptExt_FontName>
      <ScriptExt_FontSize>10</ScriptExt_FontSize>
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      <ScriptExt_ScriptTextA></ScriptExt_ScriptTextA>
      <ScriptExt_Language>IronPython</ScriptExt_Language>
      <ErrorMessage>No material stream connected to the outlet of the mixer.</ErrorMessage>
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      <ComponentName>MIST-41ccaf9f-f143-402f-b1b1-6121319ad896</ComponentName>
      <ValStatus>CAPE_VALID</ValStatus>
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      <selectedReport></selectedReport>
      <IsAdjustAttached>false</IsAdjustAttached>
      <AttachedAdjustId></AttachedAdjustId>
      <AdjustVarType>Nenhum</AdjustVarType>
      <IsSpecAttached>false</IsSpecAttached>
      <AttachedSpecId></AttachedSpecId>
      <SpecVarType>Nenhum</SpecVarType>
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      <Nome>MIST-41ccaf9f-f143-402f-b1b1-6121319ad896</Nome>
      <ShowQuickTable>false</ShowQuickTable>
      <Annotation></Annotation>
      <NodeItems />
      <PropertyPackage></PropertyPackage>
    </SimulationObject>
    <SimulationObject>
      <Type>DWSIM.DWSIM.SimulationObjects.Streams.MaterialStream</Type>
      <CompositionBasis>Mass_Fractions</CompositionBasis>
      <SpecType>Temperature_and_Pressure</SpecType>
      <IsElectrolyteStream>false</IsElectrolyteStream>
      <ReferenceSolvent></ReferenceSolvent>
      <AtEquilibrium>true</AtEquilibrium>
      <ComponentDescription>MAT-02707801-0e7c-4204-93d0-74a9bf99f660</ComponentDescription>
      <ComponentName>out</ComponentName>
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      <Descricao>CorrentedeMatria</Descricao>
      <Nome>MAT-02707801-0e7c-4204-93d0-74a9bf99f660</Nome>
      <ShowQuickTable>true</ShowQuickTable>
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      <PropertyPackage>PP-82b71c26-d8f5-45ff-840f-c8b6b4b01ca2</PropertyPackage>
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            <Compound>
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              <Nome>Metanol</Nome>
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          <Nome>Overall Liquid</Nome>
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      <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>5116</X>
      <Y>3692</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>in2</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <Name>MAT-21a3cd83-948c-47c2-9e09-68af35cbef68</Name>
      <InputConnectors>
        <Connector IsAttached="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="MIST-41ccaf9f-f143-402f-b1b1-6121319ad896" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.NodeInGraphic</Type>
      <LineWidth>2</LineWidth>
      <GradientMode>true</GradientMode>
      <LineColor>SteelBlue</LineColor>
      <Fill>true</Fill>
      <FillColor>WhiteSmoke</FillColor>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <MixPoint>true</MixPoint>
      <SplitPoint>false</SplitPoint>
      <ShapeOverride>DefaultShape</ShapeOverride>
      <Status>Calculated</Status>
      <Description>Misturador</Description>
      <Shape>0</Shape>
      <FlippedH>false</FlippedH>
      <FlippedV>false</FlippedV>
      <TipoObjeto>NodeIn</TipoObjeto>
      <IsEnergyStream>false</IsEnergyStream>
      <Active>true</Active>
      <Calculated>true</Calculated>
      <Tag>MIX-000</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <X>5221</X>
      <Y>3614</Y>
      <Name>MIST-41ccaf9f-f143-402f-b1b1-6121319ad896</Name>
      <Height>20</Height>
      <Width>20</Width>
      <Rotation>0</Rotation>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="MAT-5819667f-aaa3-477c-b5cf-9443823be855" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="MAT-21a3cd83-948c-47c2-9e09-68af35cbef68" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
        <Connector IsAttached="False" />
        <Connector IsAttached="False" />
        <Connector IsAttached="False" />
        <Connector IsAttached="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="True" ConnType="ConOut" AttachedToObjID="MAT-02707801-0e7c-4204-93d0-74a9bf99f660" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
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    <GraphicObject>
      <Type>Microsoft.MSDN.Samples.GraphicObjects.MaterialStreamGraphic</Type>
      <GradientMode>true</GradientMode>
      <GradientColor1>LightGrey</GradientColor1>
      <GradientColor2>White</GradientColor2>
      <FillColor>WhiteSmoke</FillColor>
      <LineWidth>2</LineWidth>
      <Width>20</Width>
      <Height>20</Height>
      <Rotation>0</Rotation>
      <X>5281</X>
      <Y>3614</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>out</Tag>
      <AutoSize>false</AutoSize>
      <IsConnector>false</IsConnector>
      <Name>MAT-02707801-0e7c-4204-93d0-74a9bf99f660</Name>
      <InputConnectors>
        <Connector IsAttached="True" ConnType="ConIn" AttachedFromObjID="MIST-41ccaf9f-f143-402f-b1b1-6121319ad896" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
      </InputConnectors>
      <OutputConnectors>
        <Connector IsAttached="False" />
      </OutputConnectors>
      <EnergyConnector>
        <Connector IsAttached="False" />
      </EnergyConnector>
      <SpecialConnectors />
    </GraphicObject>
  </GraphicObjects>
  <PropertyPackages>
    <PropertyPackage>
      <ID>PP-82b71c26-d8f5-45ff-840f-c8b6b4b01ca2</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>Metanol,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="Metanol" Compound2="Agua" Value="-0.0778" />
      </InteractionParameters>
    </PropertyPackage>
  </PropertyPackages>
  <Compounds>
    <Compound>
      <Type>DWSIM.DWSIM.ClassesBasicasTermodinamica.ConstantProperties</Type>
      <Name>Metanol</Name>
      <CAS_Number>67-56-1</CAS_Number>
      <Formula>CH3OH</Formula>
      <SMILES></SMILES>
      <InChI></InChI>
      <ChemicalStructure></ChemicalStructure>
      <Molar_Weight>32.042</Molar_Weight>
      <Critical_Temperature>512.6</Critical_Temperature>
      <Critical_Pressure>8095867.5</Critical_Pressure>
      <Critical_Volume>0.118</Critical_Volume>
      <Critical_Compressibility>0.224</Critical_Compressibility>
      <Acentric_Factor>0.559</Acentric_Factor>
      <Z_Rackett>0.2334</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>3.32</IG_Entropy_of_Formation_25C>
      <IG_Enthalpy_of_Formation_25C>-6270</IG_Enthalpy_of_Formation_25C>
      <IG_Gibbs_Energy_of_Formation_25C>-5065.99</IG_Gibbs_Energy_of_Formation_25C>
      <Dipole_Moment>0</Dipole_Moment>
      <Vapor_Pressure_Constant_A>79.4834234</Vapor_Pressure_Constant_A>
      <Vapor_Pressure_Constant_B>-6703.475707</Vapor_Pressure_Constant_B>
      <Vapor_Pressure_Constant_C>-8.384841112</Vapor_Pressure_Constant_C>
      <Vapor_Pressure_Constant_D>6.89E-06</Vapor_Pressure_Constant_D>
      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
      <Vapor_Pressure_TMIN>257</Vapor_Pressure_TMIN>
      <Vapor_Pressure_TMAX>364</Vapor_Pressure_TMAX>
      <Ideal_Gas_Heat_Capacity_Const_A>21.1517136</Ideal_Gas_Heat_Capacity_Const_A>
      <Ideal_Gas_Heat_Capacity_Const_B>0.070924392</Ideal_Gas_Heat_Capacity_Const_B>
      <Ideal_Gas_Heat_Capacity_Const_C>2.59E-05</Ideal_Gas_Heat_Capacity_Const_C>
      <Ideal_Gas_Heat_Capacity_Const_D>-2.85E-08</Ideal_Gas_Heat_Capacity_Const_D>
      <Ideal_Gas_Heat_Capacity_Const_E>0</Ideal_Gas_Heat_Capacity_Const_E>
      <Liquid_Viscosity_Const_A>-27.20590722</Liquid_Viscosity_Const_A>
      <Liquid_Viscosity_Const_B>3126.504917</Liquid_Viscosity_Const_B>
      <Liquid_Viscosity_Const_C>1.079640505</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>337.8</Normal_Boiling_Point>
      <ID>26</ID>
      <IsPF>0</IsPF>
      <IsHYPO>0</IsHYPO>
      <HVap_A>52810129.22</HVap_A>
      <HVap_B>0.374999142</HVap_B>
      <HVap_C>0</HVap_C>
      <HVap_D>0</HVap_D>
      <HVap_TMIN>205.04</HVap_TMIN>
      <HVap_TMAX>512.6</HVap_TMAX>
      <UNIQUAC_R>1.43</UNIQUAC_R>
      <UNIQUAC_Q>1.43</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>METHANOL</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="1" />
        <Item Name="OH" Value="1" />
      </UNIFACGroups>
      <MODFACGroups>
        <Item Name="CH3" Value="1" />
        <Item Name="OH" Value="1" />
      </MODFACGroups>
      <Elements>
        <Item Name="C" Value="1" />
        <Item Name="H" Value="4" />
        <Item Name="O" Value="1" />
      </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>
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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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&lt;/DockPanel&gt;</PanelLayout>
</DWSIM_Simulation_Data>