diff options
| author | Sashi20 | 2024-05-01 00:20:10 +0550 |
|---|---|---|
| committer | Sashi20 | 2024-05-01 00:20:10 +0550 |
| commit | beee63a35ea9b5c65aebe51f3b10ce944701c694 (patch) | |
| tree | c0ce97382ae910766f63138ae04f89108227d234 | |
| parent | 546b9fb398e5c3e30a6cab6e25ceb07140ee5530 (diff) | |
| download | DWSIM-Flowsheets-beee63a35ea9b5c65aebe51f3b10ce944701c694.tar.gz DWSIM-Flowsheets-beee63a35ea9b5c65aebe51f3b10ce944701c694.tar.bz2 DWSIM-Flowsheets-beee63a35ea9b5c65aebe51f3b10ce944701c694.zip | |
Added(A)/Deleted(D) following Flowsheet file
M Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf
M Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
A Simulation_Of_Wastewater_Treatment_Plant-Degradation_Of_Malathion_By_Ms_Atshaya_T/user_defined_compound/Alum.json
3 files changed, 2329 insertions, 2113 deletions
diff --git a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf Binary files differindex 1b2f24d..12735a8 100644 --- a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf +++ b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf diff --git a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml index 575be9f..f6c0600 100644 --- a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml +++ b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml @@ -4,76 +4,11 @@ <BuildVersion>8.6.5.0</BuildVersion>
<BuildDate>2000-01-06T00:00:00</BuildDate>
<OSInfo>Microsoft Windows 11 Home Single Language, Version 10.0.22621.0, Win32NT Platform</OSInfo>
- <SavedOn>2024-01-22T14:41:52.8927642+05:30</SavedOn>
+ <SavedOn>2024-04-13T20:29:27.0060097+05:30</SavedOn>
<SavedFromClassicUI>true</SavedFromClassicUI>
</GeneralInfo>
<SimulationObjects>
<SimulationObject>
- <Type>DWSIM.UnitOperations.SpecialOps.Recycle</Type>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <Converged>true</Converged>
- <CopyOnStreamDataError>false</CopyOnStreamDataError>
- <Errors />
- <Values />
- <IterationsTaken>2</IterationsTaken>
- <IterationCount>1</IterationCount>
- <AccelerationMethod>None</AccelerationMethod>
- <ConvergenceParameters>
- <Type>DWSIM.UnitOperations.SpecialOps.Helpers.Recycle.ConvergenceParameters</Type>
- <Temperatura>0.1</Temperatura>
- <Pressao>0.1</Pressao>
- <VazaoMassica>0.01</VazaoMassica>
- <FracaoVapor>0.01</FracaoVapor>
- <Entalpia>1</Entalpia>
- <Entropia>0.01</Entropia>
- <Composicao>0.001</Composicao>
- </ConvergenceParameters>
- <ConvergenceHistory>
- <Type>DWSIM.UnitOperations.SpecialOps.Helpers.Recycle.ConvergenceHistory</Type>
- </ConvergenceHistory>
- <MaximumIterations>50</MaximumIterations>
- <MobileCompatible>true</MobileCompatible>
- <ObjectClass>Logical</ObjectClass>
- <IsDirty>true</IsDirty>
- <CanUsePreviousResults>false</CanUsePreviousResults>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
- <ComponentDescription>Reciclo</ComponentDescription>
- <ComponentName>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</ComponentName>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</Name>
- <UserDefinedChartNames />
- <ProductName>Recycle Block</ProductName>
- <ProductDescription>Block for connecting tear Material Streams</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>8.6.5.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <IsSource>false</IsSource>
- <IsSink>false</IsSink>
- <DynamicProperties />
- <DynamicPropertiesDescriptions />
- <DynamicPropertiesUnitTypes />
- <AttachedUtilities />
- <WegPars AccelDelay="2" AccelFreq="4" Qmax="0" Qmin="-20" />
- </SimulationObject>
- <SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
<ObjectClass>Streams</ObjectClass>
<SupportsDynamicMode>true</SupportsDynamicMode>
@@ -82,11 +17,11 @@ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
<DefinedFlow>Mass</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-167.71785871462</TotalEnergyFlow>
+ <TotalEnergyFlow>-79.5539552876325</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</ComponentName>
- <Name2>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name2>
+ <ComponentName>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</ComponentName>
+ <Name2>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
@@ -106,7 +41,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:55</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -114,7 +50,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name>
+ <Name>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -140,19 +76,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.85079554049368E-10</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>48.9654943370213</Kvalue>
- <lnKvalue>3.89111585284366</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>2.25058744836356E-18</VolumetricFlow>
+ <VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -165,19 +101,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>6092.77376946324</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.540969372119056</Kvalue>
- <lnKvalue>-0.614392615196564</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>1.17847174288279E-05</VolumetricFlow>
+ <VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -190,20 +126,20 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6910.68370137748</Molarity>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>6832.55660172031</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1.40470232610445</Kvalue>
- <lnKvalue>0.339825412797292</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <Kvalue>1</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.0416666666666667</MassFlow>
+ <MolarFlow>0.415826696739254</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0.000108209266828059</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <VolumetricFlow>0.000121719210239563</VolumetricFlow>
+ <VolumetricFraction>2</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -218,27 +154,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>802.227353678979</density>
- <enthalpy>0.1263045937633</enthalpy>
- <entropy>0.000423627683257757</entropy>
+ <density>684.635836605579</density>
+ <enthalpy>0.147998387730284</enthalpy>
+ <entropy>0.000496389024753595</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0481312282239006</massflow>
- <molar_enthalpy>7.79215837322055</molar_enthalpy>
- <molar_entropy>0.0261350272454152</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
- <molecularWeight>61.6933885067027</molecularWeight>
+ <massflow>0.0416666666666667</massflow>
+ <molar_enthalpy>14.8297344473499</molar_enthalpy>
+ <molar_entropy>0.0497391730583597</molar_entropy>
+ <molarflow>0.415826696739254</molarflow>
+ <molecularWeight>100.202</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0440259158385757</surfaceTension>
+ <surfaceTension>0.0193054358083515</surfaceTension>
<temperature>298.15</temperature>
- <thermalConductivity>0.139308428645295</thermalConductivity>
- <volumetric_flow>5.99969921284445E-05</volumetric_flow>
+ <thermalConductivity>0.118010205685203</thermalConductivity>
+ <volumetric_flow>6.08596051197814E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.060170843288607</helmholtz_energy>
- <internal_energy>0.0661337504746934</internal_energy>
+ <helmholtz_energy>-0.147992905281822</helmholtz_energy>
+ <internal_energy>5.4824484624072E-06</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
- <molar_internal_energy>4.08001516144059</molar_internal_energy>
+ <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
+ <molar_internal_energy>0.000549352300830126</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -248,22 +184,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
+ <ActivityCoeff>7.17641923898794</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.85079554049368E-10</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
+ <FugacityCoeff>2.17188219124978</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>1.12529372418178E-18</VolumetricFlow>
- <VolumetricFraction>1.87558356554391E-14</VolumetricFraction>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -273,22 +209,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
+ <ActivityCoeff>1.00071619041225</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>6092.77376946324</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
+ <FugacityCoeff>0.0313434094895189</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>5.89235871441393E-06</VolumetricFlow>
- <VolumetricFraction>0.0982109020032083</VolumetricFraction>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -298,22 +234,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
+ <ActivityCoeff>1.00551404572158</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6910.68370137748</Molarity>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>6832.55660172031</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
+ <FugacityCoeff>0.0813875285498942</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <MassFlow>0.0416666666666667</MassFlow>
+ <MolarFlow>0.415826696739254</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>0</PartialPressure>
+ <PartialPressure>101325</PartialPressure>
<PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>5.41046334140295E-05</VolumetricFlow>
- <VolumetricFraction>0.901789097996773</VolumetricFraction>
+ <VolumetricFlow>6.08596051197814E-05</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -328,29 +264,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00149754502528238</compressibilityFactor>
- <density>802.227353678979</density>
- <enthalpy>0.1263045937633</enthalpy>
- <entropy>0.000423627683257757</entropy>
+ <compressibilityFactor>0.00598235873487061</compressibilityFactor>
+ <density>684.635836605579</density>
+ <enthalpy>0.147998387730284</enthalpy>
+ <entropy>0.000496389024753595</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>7.54356581787694E-07</kinematic_viscosity>
- <massflow>0.0481312282239006</massflow>
+ <kinematic_viscosity>5.07314344208017E-07</kinematic_viscosity>
+ <massflow>0.0416666666666667</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>7.79215837322055</molar_enthalpy>
- <molar_entropy>0.0261350272454152</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <molar_enthalpy>14.8297344473499</molar_enthalpy>
+ <molar_entropy>0.0497391730583597</molar_entropy>
+ <molarflow>0.415826696739254</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>61.6933885067027</molecularWeight>
- <thermalConductivity>0.139308428645295</thermalConductivity>
- <viscosity>0.000605165484337862</viscosity>
- <volumetric_flow>5.99969921284445E-05</volumetric_flow>
+ <molecularWeight>100.202</molecularWeight>
+ <thermalConductivity>0.118010205685203</thermalConductivity>
+ <viscosity>0.000347325580468866</viscosity>
+ <volumetric_flow>6.08596051197814E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.060170843288607</helmholtz_energy>
- <internal_energy>0.0661337504746934</internal_energy>
+ <helmholtz_energy>-0.147992905281822</helmholtz_energy>
+ <internal_energy>5.4824484624072E-06</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
- <molar_internal_energy>4.08001516144059</molar_internal_energy>
+ <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
+ <molar_internal_energy>0.000549352300830126</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -362,8 +298,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>7.8552689004154E-13</MassFraction>
- <MoleFraction>1.07348844110935E-12</MoleFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -372,8 +308,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>1.08771216295405E-07</PartialPressure>
- <PartialVolume>17.9016023256588</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>14.1798621355377</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
@@ -387,8 +323,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0575325219578357</MassFraction>
- <MoleFraction>0.253471356208221</MoleFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -397,8 +333,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>25682.985167798</PartialPressure>
- <PartialVolume>5.55280912123346</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>4.39838101482063</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
@@ -412,8 +348,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.942467478041379</MassFraction>
- <MoleFraction>0.746528643790706</MoleFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -422,8 +358,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>75642.0148320932</PartialPressure>
- <PartialVolume>30.8850364560437</PartialVolume>
+ <PartialPressure>101325</PartialPressure>
+ <PartialVolume>24.4640424377005</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
@@ -455,23 +391,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>9.36609665906765</ActivityCoeff>
+ <ActivityCoeff>7.17641923898794</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.85079554049368E-10</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>2.83456942214845</FugacityCoeff>
+ <FugacityCoeff>2.17188219124978</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>2.22138503385162E-09</PartialPressure>
+ <PartialPressure>0</PartialPressure>
<PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>1.12529372418178E-18</VolumetricFlow>
- <VolumetricFraction>1.87558356554391E-14</VolumetricFraction>
- <DiffusionCoefficient>2.97501551001106E-09</DiffusionCoefficient>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>5.18354190784942E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -480,23 +416,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00071619041202</ActivityCoeff>
+ <ActivityCoeff>1.00071619041225</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>6092.77376946324</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0313434094895116</FugacityCoeff>
+ <FugacityCoeff>0.0313434094895189</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>47475.8581381307</PartialPressure>
+ <PartialPressure>0</PartialPressure>
<PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>5.89235871441393E-06</VolumetricFlow>
- <VolumetricFraction>0.0982109020032083</VolumetricFraction>
- <DiffusionCoefficient>3.85296509324523E-09</DiffusionCoefficient>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>6.71324433876425E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -505,23 +441,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.00551404572164</ActivityCoeff>
+ <ActivityCoeff>1.00551404572158</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6910.68370137748</Molarity>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
+ <Molarity>6832.55660172031</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0813875285498997</FugacityCoeff>
+ <FugacityCoeff>0.0813875285498942</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <MassFlow>0.0416666666666667</MassFlow>
+ <MolarFlow>0.415826696739254</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>53849.1418618672</PartialPressure>
+ <PartialPressure>101325</PartialPressure>
<PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>5.41046334140295E-05</VolumetricFlow>
- <VolumetricFraction>0.901789097996773</VolumetricFraction>
- <DiffusionCoefficient>2.59101048628958E-09</DiffusionCoefficient>
+ <VolumetricFlow>6.08596051197814E-05</VolumetricFlow>
+ <VolumetricFraction>1</VolumetricFraction>
+ <DiffusionCoefficient>4.51446770417322E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -535,36 +471,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00149754502528238</compressibilityFactor>
- <density>802.227353678979</density>
- <enthalpy>0.1263045937633</enthalpy>
- <enthalpyF>-3484.59544673195</enthalpyF>
- <entropy>0.000423627683257757</entropy>
- <entropyF>0.000423627682931141</entropyF>
+ <compressibilityFactor>0.00598235873487061</compressibilityFactor>
+ <density>684.635836605579</density>
+ <enthalpy>0.147998387730284</enthalpy>
+ <enthalpyF>-1909.29492690318</enthalpyF>
+ <entropy>0.000496389024753595</entropy>
+ <entropyF>0.000496389024753595</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>7.54356581787694E-07</kinematic_viscosity>
- <massflow>0.0481312282239006</massflow>
+ <kinematic_viscosity>5.07314344208017E-07</kinematic_viscosity>
+ <massflow>0.0416666666666667</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>7.79215837322055</molar_enthalpy>
- <molar_entropy>0.0261350272454152</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <molar_enthalpy>14.8297344473499</molar_enthalpy>
+ <molar_entropy>0.0497391730583597</molar_entropy>
+ <molarflow>0.415826696739254</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>61.6933885067027</molecularWeight>
+ <molecularWeight>100.202</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.139308428645295</thermalConductivity>
- <viscosity>0.000605165484337862</viscosity>
- <volumetric_flow>5.99969921284445E-05</volumetric_flow>
- <bulk_modulus>-90.8938782184429</bulk_modulus>
+ <thermalConductivity>0.118010205685203</thermalConductivity>
+ <viscosity>0.000347325580468866</viscosity>
+ <volumetric_flow>6.08596051197814E-05</volumetric_flow>
+ <bulk_modulus>-2709104.05471673</bulk_modulus>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.060170843288607</helmholtz_energy>
- <internal_energy>0.0661337504746934</internal_energy>
- <isothermal_compressibility>-0.0110018410436479</isothermal_compressibility>
+ <helmholtz_energy>-0.147992905281822</helmholtz_energy>
+ <internal_energy>5.4824484624072E-06</internal_energy>
+ <isothermal_compressibility>-3.69125725628343E-07</isothermal_compressibility>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
- <molar_internal_energy>4.08001516144059</molar_internal_energy>
- <idealGasHeatCapacityCp>1.66460606324854</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.08808958782905</idealGasHeatCapacityRatio>
+ <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
+ <molar_internal_energy>0.000549352300830126</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.63261361609135</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.05354297154205</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -671,8 +607,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -696,8 +630,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -721,8 +653,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -766,8 +696,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -791,8 +719,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -816,8 +742,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -911,8 +835,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
+ <MassFraction>1</MassFraction>
+ <MoleFraction>1</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -950,149 +874,19 @@ </Phases>
</SimulationObject>
<SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
- <ObjectClass>Exchangers</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
- <OutletTemperature>298.15</OutletTemperature>
- <OutletVaporFraction>0</OutletVaporFraction>
- <CalcMode>OutletTemperature</CalcMode>
- <Eficiencia>100</Eficiencia>
- <DeltaT>-70.7602112522569</DeltaT>
- <DeltaQ>8.93828063257156</DeltaQ>
- <MobileCompatible>true</MobileCompatible>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>Resfriador</ComponentDescription>
- <ComponentName>RESF-26c14620-b257-493a-b6d0-b997b40f8564</ComponentName>
- <IsDirty>true</IsDirty>
- <CanUsePreviousResults>false</CanUsePreviousResults>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>RESF-26c14620-b257-493a-b6d0-b997b40f8564</Name>
- <UserDefinedChartNames />
- <ProductName>Cooler</ProductName>
- <ProductDescription>Simple cooler model</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>8.6.5.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <IsSource>false</IsSource>
- <IsSink>false</IsSink>
- <DynamicProperties>
- <Property>
- <Name>Flow Conductance</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>1.0</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>1.0</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>101325.0</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>-1.0</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>0.0</Data>
- </Property>
- </DynamicProperties>
- <DynamicPropertiesDescriptions>
- <Property>
- <Name>Flow Conductance</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Cooler Volume"</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Empties the volume content on the next run."</Data>
- </Property>
- </DynamicPropertiesDescriptions>
- <DynamicPropertiesUnitTypes>
- <Property>
- <Name>Flow Conductance</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>67</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>63</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>46</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>66</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>66</Data>
- </Property>
- </DynamicPropertiesUnitTypes>
- <AttachedUtilities />
- <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
- </SimulationObject>
- <SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
<ObjectClass>Streams</ObjectClass>
<SupportsDynamicMode>true</SupportsDynamicMode>
<HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
<OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
<FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mole</DefinedFlow>
+ <DefinedFlow>Mass</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-158.779578082049</TotalEnergyFlow>
- <AtEquilibrium>true</AtEquilibrium>
+ <TotalEnergyFlow>-169.129449897322</TotalEnergyFlow>
+ <AtEquilibrium>false</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</ComponentName>
- <Name2>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name2>
+ <ComponentName>MAT-db971471-1e8a-42d3-ad06-be461cacea57</ComponentName>
+ <Name2>MAT-db971471-1e8a-42d3-ad06-be461cacea57</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
@@ -1112,7 +906,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:55</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -1120,7 +915,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name>
+ <Name>MAT-db971471-1e8a-42d3-ad06-be461cacea57</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -1146,19 +941,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.6578667110063E-10</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.91616119531264E-12</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>21.5085411131849</Kvalue>
- <lnKvalue>3.0684501173247</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <Kvalue>52.3072770616318</Kvalue>
+ <lnKvalue>3.95749546177199</lnKvalue>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFlow>1.39634210549945E-20</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -1171,19 +966,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>5680.44265171835</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>7105.48027062453</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.858622129903028</Kvalue>
- <lnKvalue>-0.152426349120118</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <Kvalue>0.560637879120848</Kvalue>
+ <lnKvalue>-0.578486179908421</lnKvalue>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFlow>1.26860824662199E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -1196,19 +991,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6443.00017285851</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6849.61521335677</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1.12464517488072</Kvalue>
- <lnKvalue>0.117467585801286</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <Kvalue>1.45577434415276</Kvalue>
+ <lnKvalue>0.375731848085475</lnKvalue>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFlow>9.90010008181747E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -1224,27 +1019,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>747.936268215432</density>
- <enthalpy>185.832777551232</enthalpy>
- <entropy>0.503734436952633</entropy>
+ <density>814.352360218552</density>
+ <enthalpy>0.12442402693214</enthalpy>
+ <entropy>0.00041732023119953</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0481312282239006</massflow>
- <molar_enthalpy>11464.6537427478</molar_enthalpy>
- <molar_entropy>31.0770843231239</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
- <molecularWeight>61.6933885067027</molecularWeight>
+ <massflow>0.0454763199392864</massflow>
+ <molar_enthalpy>7.2607887288477</molar_enthalpy>
+ <molar_entropy>0.0243528047252983</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
+ <molecularWeight>58.3551980101696</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0347462890490967</surfaceTension>
- <temperature>368.910211252257</temperature>
- <thermalConductivity>0.120307882424234</thermalConductivity>
- <volumetric_flow>6.43520447788168E-05</volumetric_flow>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.0659014819911475</helmholtz_energy>
- <internal_energy>185.766876069241</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-4.06568573164734</molar_helmholtz_energy>
- <molar_internal_energy>11460.5880570162</molar_internal_energy>
+ <surfaceTension>0.0461688565551219</surfaceTension>
+ <temperature>298.15</temperature>
+ <thermalConductivity>0.143299726742525</thermalConductivity>
+ <volumetric_flow>5.58435416421973E-05</volumetric_flow>
+ <gibbs_free_energy>1.38777878078145E-17</gibbs_free_energy>
+ <helmholtz_energy>-0.0599408772157934</helmholtz_energy>
+ <internal_energy>0.0644831497163465</internal_energy>
+ <molar_gibbs_free_energy>8.0984105546813E-16</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-3.49786175883089</molar_helmholtz_energy>
+ <molar_internal_energy>3.76292697001681</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -1256,21 +1051,21 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054608E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.6578667110063E-10</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.91616119531264E-12</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>9.9338071798953E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0829883956543016</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <PartialVolume>0.0737984191993252</PartialVolume>
+ <VolumetricFlow>6.98171052749727E-21</VolumetricFlow>
+ <VolumetricFraction>1.25022703112756E-16</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1281,20 +1076,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.468550290038299</MoleFraction>
- <Molarity>5680.44265171834</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>7105.48027062453</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00658545137293009</MassFlow>
- <MolarFlow>0.365548099886879</MolarFlow>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0187413369026188</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <PartialVolume>0.0180809547091451</PartialVolume>
+ <VolumetricFlow>6.34304123310997E-06</VolumetricFlow>
+ <VolumetricFraction>0.113585941123708</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -1306,21 +1101,21 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.531449709961679</MoleFraction>
- <Molarity>6443.0001728585</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6849.61521335677</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0415457768509694</MassFlow>
- <MolarFlow>0.414620235633714</MolarFlow>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.160163998201726</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <PartialVolume>0.146372899520274</PartialVolume>
+ <VolumetricFlow>4.95005004090874E-05</VolumetricFlow>
+ <VolumetricFraction>0.886414058876292</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1334,29 +1129,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00132557135008417</compressibilityFactor>
- <density>747.936268215431</density>
- <enthalpy>185.832777551233</enthalpy>
- <entropy>0.503734436952634</entropy>
+ <compressibilityFactor>0.00141110005116182</compressibilityFactor>
+ <density>814.352360218552</density>
+ <enthalpy>0.12442402693214</enthalpy>
+ <entropy>0.00041732023119953</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>3.12547653408567E-07</kinematic_viscosity>
- <massflow>0.0481312282239005</massflow>
- <massfraction>0.999999999999998</massfraction>
- <molar_enthalpy>11464.6537427478</molar_enthalpy>
- <molar_entropy>31.0770843231239</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <kinematic_viscosity>7.70571617225547E-07</kinematic_viscosity>
+ <massflow>0.0454763199392864</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>7.2607887288477</molar_enthalpy>
+ <molar_entropy>0.0243528047252983</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>61.6933885067026</molecularWeight>
- <thermalConductivity>0.120307882424234</thermalConductivity>
- <viscosity>0.000233765725529893</viscosity>
- <volumetric_flow>6.43520447788168E-05</volumetric_flow>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.0659014819911476</helmholtz_energy>
- <internal_energy>185.766876069242</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-4.06568573164734</molar_helmholtz_energy>
- <molar_internal_energy>11460.5880570162</molar_internal_energy>
+ <molecularWeight>58.3551980101696</molecularWeight>
+ <thermalConductivity>0.143299726742525</thermalConductivity>
+ <viscosity>0.000627516815205051</viscosity>
+ <volumetric_flow>5.58435416421973E-05</volumetric_flow>
+ <gibbs_free_energy>1.38777878078145E-17</gibbs_free_energy>
+ <helmholtz_energy>-0.0599408772157934</helmholtz_energy>
+ <internal_energy>0.0644831497163465</internal_energy>
+ <molar_gibbs_free_energy>8.0984105546813E-16</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-3.49786175883089</molar_helmholtz_energy>
+ <molar_internal_energy>3.76292697001681</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -1368,8 +1163,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>4.07917369751543E-13</MassFraction>
- <MoleFraction>4.71539613410424E-13</MoleFraction>
+ <MassFraction>5.43567536296924E-15</MassFraction>
+ <MoleFraction>7.18226361496533E-15</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -1378,11 +1173,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>26.1859358578682</PartialVolume>
+ <PartialPressure>7.27742860786362E-10</PartialPressure>
+ <PartialVolume>18.5148582516745</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>5.87219541532721E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1393,8 +1188,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.107952609231912</MassFraction>
- <MoleFraction>0.402307647999366</MoleFraction>
+ <MassFraction>0.0670125388927785</MassFraction>
+ <MoleFraction>0.2854585548075</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -1403,11 +1198,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>8.12248539736532</PartialVolume>
+ <PartialPressure>28924.0880658699</PartialPressure>
+ <PartialVolume>5.74303193133071</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>3.14909481177876E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1418,8 +1213,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.89204739076768</MassFraction>
- <MoleFraction>0.597692352000162</MoleFraction>
+ <MassFraction>0.932987461107216</MassFraction>
+ <MoleFraction>0.714541445192493</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -1428,11 +1223,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>45.1777203455511</PartialVolume>
+ <PartialPressure>72400.9119341294</PartialPressure>
+ <PartialVolume>31.9430664182405</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.65025205694262E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1452,8 +1247,6 @@ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
<molar_helmholtz_energy>0</molar_helmholtz_energy>
<molar_internal_energy>0</molar_internal_energy>
- <idealGasHeatCapacityCp>1.96382536092348</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.0631930833244</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -1463,23 +1256,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>6.52554770166032</ActivityCoeff>
+ <ActivityCoeff>9.65375432670081</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054608E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.6578667110063E-10</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.91616119531264E-12</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>21.5085411141129</FugacityCoeff>
+ <FugacityCoeff>2.92162656648511</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>9.9338071798953E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>2.22138503385161E-09</PartialPressure>
- <PartialVolume>-0.0829883956543016</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <PartialPressure>1.39128416095697E-11</PartialPressure>
+ <PartialVolume>0.0737984191993252</PartialVolume>
+ <VolumetricFlow>6.98171052749727E-21</VolumetricFlow>
+ <VolumetricFraction>1.25022703112756E-16</VolumetricFraction>
+ <DiffusionCoefficient>2.86850451170521E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1488,23 +1281,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00008758260384</ActivityCoeff>
+ <ActivityCoeff>1.00071619041199</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.468550290038299</MoleFraction>
- <Molarity>5680.44265171834</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>7105.48027062453</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.858622129940072</FugacityCoeff>
+ <FugacityCoeff>0.0313434094895109</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00658545137293009</MassFlow>
- <MolarFlow>0.365548099886879</MolarFlow>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
- <PartialPressure>47475.8581381307</PartialPressure>
- <PartialVolume>0.0187413369026188</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>1.20788816448314E-08</DiffusionCoefficient>
+ <PartialPressure>51591.3910619571</PartialPressure>
+ <PartialVolume>0.0180809547091451</PartialVolume>
+ <VolumetricFlow>6.34304123310997E-06</VolumetricFlow>
+ <VolumetricFraction>0.113585941123708</VolumetricFraction>
+ <DiffusionCoefficient>3.71502189357511E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1513,23 +1306,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.00065583232412</ActivityCoeff>
+ <ActivityCoeff>1.00551404572167</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.531449709961679</MoleFraction>
- <Molarity>6443.0001728585</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6849.61521335677</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>1.12464517492925</FugacityCoeff>
+ <FugacityCoeff>0.0813875285499013</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0415457768509694</MassFlow>
- <MolarFlow>0.414620235633714</MolarFlow>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>53849.1418618671</PartialPressure>
- <PartialVolume>-0.160163998201726</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <PartialPressure>49733.6089380429</PartialPressure>
+ <PartialVolume>0.146372899520274</PartialVolume>
+ <VolumetricFlow>4.95005004090874E-05</VolumetricFlow>
+ <VolumetricFraction>0.886414058876292</VolumetricFraction>
+ <DiffusionCoefficient>2.49824757040327E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1543,36 +1336,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00132557135008417</compressibilityFactor>
- <density>747.936268215431</density>
- <enthalpy>185.832777551233</enthalpy>
- <enthalpyF>-3298.88897377448</enthalpyF>
- <entropy>0.503734436952634</entropy>
- <entropyF>0.503734436952307</entropyF>
+ <compressibilityFactor>0.00141110005116182</compressibilityFactor>
+ <density>814.352360218552</density>
+ <enthalpy>0.12442402693214</enthalpy>
+ <enthalpyF>-3719.07826130637</enthalpyF>
+ <entropy>0.00041732023119953</entropy>
+ <entropyF>0.000417320231197368</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>3.12547653408567E-07</kinematic_viscosity>
- <massflow>0.0481312282239005</massflow>
- <massfraction>0.999999999999998</massfraction>
- <molar_enthalpy>11464.6537427478</molar_enthalpy>
- <molar_entropy>31.0770843231239</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <kinematic_viscosity>7.70571617225547E-07</kinematic_viscosity>
+ <massflow>0.0454763199392864</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>7.2607887288477</molar_enthalpy>
+ <molar_entropy>0.0243528047252983</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>61.6933885067026</molecularWeight>
+ <molecularWeight>58.3551980101696</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.120307882424234</thermalConductivity>
- <viscosity>0.000233765725529893</viscosity>
- <volumetric_flow>6.43520447788168E-05</volumetric_flow>
- <bulk_modulus>-94.6317497974457</bulk_modulus>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.0659014819911476</helmholtz_energy>
- <internal_energy>185.766876069242</internal_energy>
- <isothermal_compressibility>-0.010567277918251</isothermal_compressibility>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-4.06568573164734</molar_helmholtz_energy>
- <molar_internal_energy>11460.5880570162</molar_internal_energy>
- <idealGasHeatCapacityCp>1.96166961448807</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.07376580750886</idealGasHeatCapacityRatio>
+ <thermalConductivity>0.143299726742525</thermalConductivity>
+ <viscosity>0.000627516815205051</viscosity>
+ <volumetric_flow>5.58435416421973E-05</volumetric_flow>
+ <bulk_modulus>-92.8642458102608</bulk_modulus>
+ <gibbs_free_energy>1.38777878078145E-17</gibbs_free_energy>
+ <helmholtz_energy>-0.0599408772157934</helmholtz_energy>
+ <internal_energy>0.0644831497163465</internal_energy>
+ <isothermal_compressibility>-0.0107684070577948</isothermal_compressibility>
+ <molar_gibbs_free_energy>8.0984105546813E-16</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-3.49786175883089</molar_helmholtz_energy>
+ <molar_internal_energy>3.76292697001681</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.66936815283335</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.09330846846733</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -1594,11 +1387,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0829883956543016</PartialVolume>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1619,8 +1412,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0187413369026188</PartialVolume>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -1644,11 +1437,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.160163998201726</PartialVolume>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1690,10 +1483,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0829883956543016</PartialVolume>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1715,7 +1508,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0187413369026188</PartialVolume>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -1740,10 +1533,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.160163998201726</PartialVolume>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1785,10 +1578,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0829883956543016</PartialVolume>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1810,7 +1603,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0187413369026188</PartialVolume>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -1835,10 +1628,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.160163998201726</PartialVolume>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1880,10 +1673,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0829883956543016</PartialVolume>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1905,7 +1698,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0187413369026188</PartialVolume>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -1930,10 +1723,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.160163998201726</PartialVolume>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -1958,65 +1751,19 @@ </Phases>
</SimulationObject>
<SimulationObject>
- <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
- <ObjectClass>Streams</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <ComponentDescription>CorrentedeEnergia</ComponentDescription>
- <ComponentName>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</ComponentName>
- <EnergyFlow>8.93828063257156</EnergyFlow>
- <MobileCompatible>true</MobileCompatible>
- <Name2>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name2>
- <code>0</code>
- <IsDirty>true</IsDirty>
- <CanUsePreviousResults>false</CanUsePreviousResults>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name>
- <UserDefinedChartNames />
- <ProductName>Energy Stream</ProductName>
- <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>8.6.5.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <IsSource>false</IsSource>
- <IsSink>false</IsSink>
- <DynamicProperties />
- <DynamicPropertiesDescriptions />
- <DynamicPropertiesUnitTypes />
- <AttachedUtilities />
- </SimulationObject>
- <SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
<ObjectClass>Streams</ObjectClass>
<SupportsDynamicMode>true</SupportsDynamicMode>
<HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
<OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
<FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mole</DefinedFlow>
+ <DefinedFlow>Mass</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-154.291636193291</TotalEnergyFlow>
+ <TotalEnergyFlow>-166.710668180743</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</ComponentName>
- <Name2>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name2>
+ <ComponentName>MAT-9f510731-7729-4083-8c48-1c157b4ee026</ComponentName>
+ <Name2>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
@@ -2036,7 +1783,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:55</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -2044,7 +1792,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name>
+ <Name>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -2070,20 +1818,20 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.353390589738737</MassFraction>
- <MoleFraction>0.46790357445438</MoleFraction>
- <Molarity>4312.42913406151</Molarity>
+ <MassFraction>0.763250971621835</MassFraction>
+ <MoleFraction>0.5</MoleFraction>
+ <Molarity>11556.5422306547</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1.61258634580789</Kvalue>
- <lnKvalue>0.477839316041996</lnKvalue>
- <MassFlow>0.0212014156130144</MassFlow>
- <MolarFlow>0.365043552866217</MolarFlow>
+ <Kvalue>1.79548461964337</Kvalue>
+ <lnKvalue>0.585274968589596</lnKvalue>
+ <MassFlow>0.0212014158783843</MassFlow>
+ <MolarFlow>0.365043557435326</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>-0.000158396019674656</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <VolumetricFlow>5.07429608938773E-05</VolumetricFlow>
+ <VolumetricFraction>1.60641972316535</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -2095,20 +1843,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0102429381170448</MassFraction>
- <MoleFraction>0.043722510590787</MoleFraction>
- <Molarity>402.968130144956</Molarity>
+ <MassFraction>0.236749028378165</MassFraction>
+ <MoleFraction>0.5</MoleFraction>
+ <Molarity>11556.5422306547</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.291484400663683</Kvalue>
- <lnKvalue>-1.23276878864176</lnKvalue>
- <MassFlow>0.000614517744454951</MassFlow>
- <MolarFlow>0.0341109183123965</MolarFlow>
+ <Kvalue>0.204515380356629</Kvalue>
+ <lnKvalue>-1.58711209675951</lnKvalue>
+ <MassFlow>0.00657636189939348</MassFlow>
+ <MolarFlow>0.365043557435326</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>3.49329705236692E-06</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <VolumetricFlow>1.24322605779949E-05</VolumetricFlow>
+ <VolumetricFraction>0.393580276834651</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -2120,19 +1868,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.636366472144218</MassFraction>
- <MoleFraction>0.48837391495483</MoleFraction>
- <Molarity>4501.09384529232</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.47652146799572</Kvalue>
- <lnKvalue>-0.741242503396525</lnKvalue>
- <MassFlow>0.0381783512347965</MassFlow>
- <MolarFlow>0.381013864341994</MolarFlow>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0.000324201065397565</VolumetricFlow>
+ <VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -2148,27 +1896,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>708.740364598857</density>
- <enthalpy>93.2778591049466</enthalpy>
- <entropy>0.281905762245771</entropy>
+ <density>879.388378247172</density>
+ <enthalpy>10.867318406018</enthalpy>
+ <entropy>0.0364491645346906</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0599942845922659</massflow>
- <molar_enthalpy>7172.98840584848</molar_enthalpy>
- <molar_entropy>21.6783144846381</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
- <molecularWeight>76.8991535041362</molecularWeight>
+ <massflow>0.0277777777777778</massflow>
+ <molar_enthalpy>413.471145530632</molar_enthalpy>
+ <molar_entropy>1.38678901737593</molar_entropy>
+ <molarflow>0.730087114870652</molarflow>
+ <molecularWeight>38.04721</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0197031957424113</surfaceTension>
- <temperature>330.883123359589</temperature>
- <thermalConductivity>0.12201792032145</thermalConductivity>
- <volumetric_flow>8.46491713876383E-05</volumetric_flow>
+ <surfaceTension>0.0475505128088451</surfaceTension>
+ <temperature>298.15</temperature>
+ <thermalConductivity>0.211684674125455</thermalConductivity>
+ <volumetric_flow>3.15876107359361E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.124761576248531</helmholtz_energy>
- <internal_energy>93.1530975286981</internal_energy>
+ <helmholtz_energy>-0.085641233109552</helmholtz_energy>
+ <internal_energy>10.7816771729085</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-9.59405960335381</molar_helmholtz_energy>
- <molar_internal_energy>7163.39434624513</molar_internal_energy>
+ <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
+ <molar_internal_energy>410.212735549854</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -2178,23 +1926,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
+ <ActivityCoeff>1.50165678404913</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.353390589738737</MassFraction>
- <MoleFraction>0.467903574454381</MoleFraction>
- <Molarity>4312.42913406153</Molarity>
+ <MassFraction>0.763250971621835</MassFraction>
+ <MoleFraction>0.5</MoleFraction>
+ <Molarity>11556.5422306547</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
+ <FugacityCoeff>0.454463642386878</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0212014156130145</MassFlow>
- <MolarFlow>0.365043552866219</MolarFlow>
+ <MassFlow>0.0212014158783843</MassFlow>
+ <MolarFlow>0.365043557435326</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0775826295199718</PartialVolume>
- <VolumetricFlow>-7.91980098373278E-05</VolumetricFlow>
- <VolumetricFraction>-0.93560289532726</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <PartialPressure>50662.5</PartialPressure>
+ <PartialVolume>0.0737984191993252</PartialVolume>
+ <VolumetricFlow>2.53714804469386E-05</VolumetricFlow>
+ <VolumetricFraction>0.803209861582674</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2203,22 +1951,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
+ <ActivityCoeff>1.68270859296819</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0102429381170448</MassFraction>
- <MoleFraction>0.0437225105907871</MoleFraction>
- <Molarity>402.968130144958</Molarity>
+ <MassFraction>0.236749028378165</MassFraction>
+ <MoleFraction>0.5</MoleFraction>
+ <Molarity>11556.5422306547</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
+ <FugacityCoeff>0.0527040783253512</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.000614517744454953</MassFlow>
- <MolarFlow>0.0341109183123966</MolarFlow>
+ <MassFlow>0.00657636189939348</MassFlow>
+ <MolarFlow>0.365043557435326</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183107873823241</PartialVolume>
- <VolumetricFlow>1.74664852618346E-06</VolumetricFlow>
- <VolumetricFraction>0.0206339707471553</VolumetricFraction>
+ <PartialPressure>50662.5</PartialPressure>
+ <PartialVolume>0.0180809547091451</PartialVolume>
+ <VolumetricFlow>6.21613028899747E-06</VolumetricFlow>
+ <VolumetricFraction>0.196790138417326</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -2228,22 +1976,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
+ <ActivityCoeff>1.70977396256326</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.636366472144218</MassFraction>
- <MoleFraction>0.488373914954831</MoleFraction>
- <Molarity>4501.09384529234</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
+ <FugacityCoeff>0.138391181887592</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0381783512347966</MassFlow>
- <MolarFlow>0.381013864341995</MolarFlow>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152138304641278</PartialVolume>
- <VolumetricFlow>0.000162100532698783</VolumetricFlow>
- <VolumetricFraction>1.9149689245801</VolumetricFraction>
+ <PartialVolume>0.146372899520274</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -2258,29 +2006,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00348752858101998</compressibilityFactor>
- <density>708.740364598859</density>
- <enthalpy>93.2778591049463</enthalpy>
- <entropy>0.281905762245771</entropy>
+ <compressibilityFactor>0.00131450091730295</compressibilityFactor>
+ <density>879.388378247172</density>
+ <enthalpy>10.867318406018</enthalpy>
+ <entropy>0.0364491645346906</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>3.55602750626295E-07</kinematic_viscosity>
- <massflow>0.059994284592266</massflow>
+ <kinematic_viscosity>6.85051893836374E-07</kinematic_viscosity>
+ <massflow>0.0277777777777778</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>7172.98840584848</molar_enthalpy>
- <molar_entropy>21.6783144846381</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <molar_enthalpy>413.471145530632</molar_enthalpy>
+ <molar_entropy>1.38678901737593</molar_entropy>
+ <molarflow>0.730087114870652</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>76.8991535041365</molecularWeight>
- <thermalConductivity>0.12201792032145</thermalConductivity>
- <viscosity>0.000252030023131238</viscosity>
- <volumetric_flow>8.46491713876383E-05</volumetric_flow>
+ <molecularWeight>38.04721</molecularWeight>
+ <thermalConductivity>0.211684674125455</thermalConductivity>
+ <viscosity>0.000602426673935923</viscosity>
+ <volumetric_flow>3.15876107359361E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.124761576248531</helmholtz_energy>
- <internal_energy>93.1530975286978</internal_energy>
+ <helmholtz_energy>-0.085641233109552</helmholtz_energy>
+ <internal_energy>10.7816771729085</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-9.59405960335381</molar_helmholtz_energy>
- <molar_internal_energy>7163.39434624513</molar_internal_energy>
+ <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
+ <molar_internal_energy>410.212735549854</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -2292,8 +2040,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.650464936810833</MassFraction>
- <MoleFraction>0.75453491531984</MoleFraction>
+ <MassFraction>0.965873983786056</MassFraction>
+ <MoleFraction>0.897742309821686</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -2302,11 +2050,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>23.4052117297934</PartialVolume>
+ <PartialPressure>90963.7395426823</PartialPressure>
+ <PartialVolume>26.3206733940236</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>4.85422491385702E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2317,8 +2065,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.00340789180846115</MassFraction>
- <MoleFraction>0.0127444297950671</MoleFraction>
+ <MassFraction>0.0341260162139435</MassFraction>
+ <MoleFraction>0.102257690178314</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -2327,11 +2075,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>7.25994638990027</PartialVolume>
+ <PartialPressure>10361.2604573177</PartialPressure>
+ <PartialVolume>8.16427896456258</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.60318559078173E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2342,8 +2090,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.346127171380706</MassFraction>
- <MoleFraction>0.232720654885093</MoleFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -2353,10 +2101,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>40.3802299026597</PartialVolume>
+ <PartialVolume>45.4101785155212</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.19081938745304E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2385,23 +2133,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>1.52743555608834</ActivityCoeff>
+ <ActivityCoeff>1.50165678404913</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.353390589738737</MassFraction>
- <MoleFraction>0.467903574454381</MoleFraction>
- <Molarity>4312.42913406153</Molarity>
+ <MassFraction>0.763250971621835</MassFraction>
+ <MoleFraction>0.5</MoleFraction>
+ <Molarity>11556.5422306547</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>1.61258638235274</FugacityCoeff>
+ <FugacityCoeff>0.454463642386878</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0212014156130145</MassFlow>
- <MolarFlow>0.365043552866219</MolarFlow>
+ <MassFlow>0.0212014158783843</MassFlow>
+ <MolarFlow>0.365043557435326</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>47410.3296815902</PartialPressure>
- <PartialVolume>-0.0775826295199718</PartialVolume>
- <VolumetricFlow>-7.91980098373278E-05</VolumetricFlow>
- <VolumetricFraction>-0.93560289532726</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <PartialPressure>50662.5</PartialPressure>
+ <PartialVolume>0.0737984191993252</PartialVolume>
+ <VolumetricFlow>2.53714804469386E-05</VolumetricFlow>
+ <VolumetricFraction>0.803209861582674</VolumetricFraction>
+ <DiffusionCoefficient>2.98854081321769E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2410,23 +2158,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.64376537826977</ActivityCoeff>
+ <ActivityCoeff>1.68270859296819</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0102429381170448</MassFraction>
- <MoleFraction>0.0437225105907871</MoleFraction>
- <Molarity>402.968130144958</Molarity>
+ <MassFraction>0.236749028378165</MassFraction>
+ <MoleFraction>0.5</MoleFraction>
+ <Molarity>11556.5422306547</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.291484407269379</FugacityCoeff>
+ <FugacityCoeff>0.0527040783253512</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.000614517744454953</MassFlow>
- <MolarFlow>0.0341109183123966</MolarFlow>
+ <MassFlow>0.00657636189939348</MassFlow>
+ <MolarFlow>0.365043557435326</MolarFlow>
<Name>Water</Name>
- <PartialPressure>4430.18338561151</PartialPressure>
- <PartialVolume>0.0183107873823241</PartialVolume>
- <VolumetricFlow>1.74664852618346E-06</VolumetricFlow>
- <VolumetricFraction>0.0206339707471553</VolumetricFraction>
- <DiffusionCoefficient>1.01897927557463E-08</DiffusionCoefficient>
+ <PartialPressure>50662.5</PartialPressure>
+ <PartialVolume>0.0180809547091451</PartialVolume>
+ <VolumetricFlow>6.21613028899747E-06</VolumetricFlow>
+ <VolumetricFraction>0.196790138417326</VolumetricFraction>
+ <DiffusionCoefficient>3.87048181574814E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2435,23 +2183,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.47523255813548</ActivityCoeff>
+ <ActivityCoeff>1.70977396256326</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.636366472144218</MassFraction>
- <MoleFraction>0.488373914954831</MoleFraction>
- <Molarity>4501.09384529234</Molarity>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.476521478794775</FugacityCoeff>
+ <FugacityCoeff>0.138391181887592</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0381783512347966</MassFlow>
- <MolarFlow>0.381013864341995</MolarFlow>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>49484.4869327983</PartialPressure>
- <PartialVolume>0.152138304641278</PartialVolume>
- <VolumetricFlow>0.000162100532698783</VolumetricFlow>
- <VolumetricFraction>1.9149689245801</VolumetricFraction>
- <DiffusionCoefficient>6.74627602514587E-09</DiffusionCoefficient>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.146372899520274</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>2.60278998872266E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2465,36 +2213,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00348752858101998</compressibilityFactor>
- <density>708.740364598859</density>
- <enthalpy>93.2778591049463</enthalpy>
- <enthalpyF>-2571.77224867153</enthalpyF>
- <entropy>0.281905762245771</entropy>
- <entropyF>-5.31057424362785</entropyF>
+ <compressibilityFactor>0.00131450091730295</compressibilityFactor>
+ <density>879.388378247172</density>
+ <enthalpy>10.867318406018</enthalpy>
+ <enthalpyF>-6001.58405450675</enthalpyF>
+ <entropy>0.0364491645346906</entropy>
+ <entropyF>-12.0421571204103</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>3.55602750626295E-07</kinematic_viscosity>
- <massflow>0.059994284592266</massflow>
+ <kinematic_viscosity>6.85051893836374E-07</kinematic_viscosity>
+ <massflow>0.0277777777777778</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>7172.98840584848</molar_enthalpy>
- <molar_entropy>21.6783144846381</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <molar_enthalpy>413.471145530632</molar_enthalpy>
+ <molar_entropy>1.38678901737593</molar_entropy>
+ <molarflow>0.730087114870652</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>76.8991535041365</molecularWeight>
+ <molecularWeight>38.04721</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.12201792032145</thermalConductivity>
- <viscosity>0.000252030023131238</viscosity>
- <volumetric_flow>8.46491713876383E-05</volumetric_flow>
- <bulk_modulus>-684.702940051689</bulk_modulus>
+ <thermalConductivity>0.211684674125455</thermalConductivity>
+ <viscosity>0.000602426673935923</viscosity>
+ <volumetric_flow>3.15876107359361E-05</volumetric_flow>
+ <bulk_modulus>-289.229991511354</bulk_modulus>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.124761576248531</helmholtz_energy>
- <internal_energy>93.1530975286978</internal_energy>
- <isothermal_compressibility>-0.00146048737562673</isothermal_compressibility>
+ <helmholtz_energy>-0.085641233109552</helmholtz_energy>
+ <internal_energy>10.7816771729085</internal_energy>
+ <isothermal_compressibility>-0.00345745610534565</isothermal_compressibility>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-9.59405960335381</molar_helmholtz_energy>
- <molar_internal_energy>7163.39434624513</molar_internal_energy>
- <idealGasHeatCapacityCp>1.64827638256005</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.07019762311817</idealGasHeatCapacityRatio>
+ <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
+ <molar_internal_energy>410.212735549854</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.42364663566974</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.18132337598044</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -2516,11 +2264,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0775826295199718</PartialVolume>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2541,8 +2289,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183107873823241</PartialVolume>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2566,8 +2314,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.152138304641278</PartialVolume>
+ <PartialPressure>NaN</PartialPressure>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2601,8 +2349,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -2612,10 +2358,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0775826295199718</PartialVolume>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2626,8 +2372,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -2637,7 +2381,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183107873823241</PartialVolume>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2651,8 +2395,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -2662,7 +2404,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152138304641278</PartialVolume>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2696,8 +2438,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -2707,10 +2447,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0775826295199718</PartialVolume>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2721,8 +2461,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -2732,7 +2470,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183107873823241</PartialVolume>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2746,8 +2484,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -2757,7 +2493,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152138304641278</PartialVolume>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2802,10 +2538,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0775826295199718</PartialVolume>
+ <PartialVolume>0.0737984191993252</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -2827,7 +2563,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183107873823241</PartialVolume>
+ <PartialVolume>0.0180809547091451</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2852,7 +2588,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152138304641278</PartialVolume>
+ <PartialVolume>0.146372899520274</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -2880,93 +2616,16 @@ </Phases>
</SimulationObject>
<SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.CapeOpenUO</Type>
- <ObjectClass>CAPEOPEN</ObjectClass>
- <EmbeddedImageData></EmbeddedImageData>
- <UseEmbeddedImage>false</UseEmbeddedImage>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <ReactionSetID>DefaultSet</ReactionSetID>
- <ReactionSetName></ReactionSetName>
- <RecalcOutputStreams>true</RecalcOutputStreams>
- <MobileCompatible>false</MobileCompatible>
- <ProductName>ChemSep Column / Flash</ProductName>
- <ProductDescription>ChemSep CAPE-OPEN Unit Operation</ProductDescription>
- <ProductAuthor>Copyright (C) Ross Taylor and Harry Kooijman 2020</ProductAuthor>
- <ProductContactInfo></ProductContactInfo>
- <ProductPage>http://www.chemsep.com/</ProductPage>
- <ProductVersion>2.0.0.10</ProductVersion>
- <ProductAssembly>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</ProductAssembly>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>CapeOpenUnitOperation</ComponentDescription>
- <ComponentName>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</ComponentName>
- <IsDirty>true</IsDirty>
- <CanUsePreviousResults>false</CanUsePreviousResults>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</Name>
- <UserDefinedChartNames />
- <IsSource>false</IsSource>
- <IsSink>false</IsSink>
- <DynamicProperties />
- <DynamicPropertiesDescriptions />
- <DynamicPropertiesUnitTypes />
- <AttachedUtilities />
- <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
- <CAPEOPEN_Object_Info>
- <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.CapeOpen.CapeOpenUnitOpInfo</Type>
- <TypeName>ChemSepUO.ChemSep_UnitOperation.1</TypeName>
- <Version>2.0.0.10</Version>
- <Description>ChemSep CAPE-OPEN Unit Operation</Description>
- <HelpURL></HelpURL>
- <VendorURL>http://www.chemsep.com/</VendorURL>
- <AboutInfo>Copyright (C) Ross Taylor and Harry Kooijman 2020</AboutInfo>
- <CapeVersion>1.0</CapeVersion>
- <Location>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</Location>
- <Name>ChemSep Column / Flash</Name>
- <ImplementedCategory></ImplementedCategory>
- </CAPEOPEN_Object_Info>
- 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- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.CapeOpenUO</Type>
- <ObjectClass>CAPEOPEN</ObjectClass>
- <EmbeddedImageData></EmbeddedImageData>
- <UseEmbeddedImage>false</UseEmbeddedImage>
+ <Type>DWSIM.UnitOperations.UnitOperations.Mixer</Type>
+ <ObjectClass>MixersSplitters</ObjectClass>
<SupportsDynamicMode>true</SupportsDynamicMode>
<HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <ReactionSetID>DefaultSet</ReactionSetID>
- <ReactionSetName></ReactionSetName>
- <RecalcOutputStreams>true</RecalcOutputStreams>
- <MobileCompatible>false</MobileCompatible>
- <ProductName>ChemSep Column / Flash</ProductName>
- <ProductDescription>ChemSep CAPE-OPEN Unit Operation</ProductDescription>
- <ProductAuthor>Copyright (C) Ross Taylor and Harry Kooijman 2020</ProductAuthor>
- <ProductContactInfo></ProductContactInfo>
- <ProductPage>http://www.chemsep.com/</ProductPage>
- <ProductVersion>2.0.0.10</ProductVersion>
- <ProductAssembly>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</ProductAssembly>
+ <PressureCalculation>Minimum</PressureCalculation>
+ <MobileCompatible>true</MobileCompatible>
<ExternalSolverID></ExternalSolverID>
<ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>CapeOpenUnitOperation</ComponentDescription>
- <ComponentName>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</ComponentName>
+ <ComponentDescription>Misturador</ComponentDescription>
+ <ComponentName>MIST-ae80e666-b984-4270-b427-05f406124fe0</ComponentName>
<IsDirty>true</IsDirty>
<CanUsePreviousResults>false</CanUsePreviousResults>
<DynamicsSpec>Pressure</DynamicsSpec>
@@ -2978,7 +2637,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:26</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:55</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -2986,8 +2646,15 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</Name>
+ <Name>MIST-ae80e666-b984-4270-b427-05f406124fe0</Name>
<UserDefinedChartNames />
+ <ProductName>Stream Mixer</ProductName>
+ <ProductDescription>Mixes multiple Material Streams into a single one</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.6.5.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
<IsSource>false</IsSource>
<IsSink>false</IsSink>
<DynamicProperties />
@@ -2995,21 +2662,6 @@ <DynamicPropertiesUnitTypes />
<AttachedUtilities />
<PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
- <CAPEOPEN_Object_Info>
- <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.CapeOpen.CapeOpenUnitOpInfo</Type>
- <TypeName>ChemSepUO.ChemSep_UnitOperation.1</TypeName>
- <Version>2.0.0.10</Version>
- <Description>ChemSep CAPE-OPEN Unit Operation</Description>
- <HelpURL></HelpURL>
- <VendorURL>http://www.chemsep.com/</VendorURL>
- <AboutInfo>Copyright (C) Ross Taylor and Harry Kooijman 2020</AboutInfo>
- <CapeVersion>1.0</CapeVersion>
- <Location>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</Location>
- <Name>ChemSep Column / Flash</Name>
- <ImplementedCategory></ImplementedCategory>
- </CAPEOPEN_Object_Info>
- 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wBMAC0AMQAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAEMAYQBwAGUALQBPAHAAZQBuACAAdQBuAGkAdAAgAGkAZAA6ACAAQwBTAF8ANABfADYANwBCADQAXwAxAEQAQQAxADQARABBAF8ARABCADgANAAyAEUAQgAwACAAIAAgACAAIAAgAA0ACgBDAGEAcABlAC0ATwBwAGUAbgAgAHIAdQBuACAAbABlAHYAZQBsADoAIABuAG8AcgBtAGEAbAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgAA0ACgBDAGEAcABlAC0ATwBwAGUAbgAgAEkAbgBpAHQAaQBhAGwAaQB6AGUAZAANAAoAQwBhAHAAZQAtAE8AcABlAG4AIABUAGgAZQByAG0AbwBkAHkAbgBhAG0AaQBjAC0AcAByAG8AcABlAHIAdABpAGUAcwAgAGQAaQBzAGEAYgBsAGUAZAANAAoAUgBlAGEAZABpAG4AZwAgAGMAbwBuAGYAaQBnAHUAcgBhAHQAaQBvAG4ADQAKAFIAZQBhAGQAaQBuAGcAIABjAG8AbQBwAG8AbgBlAG4AdAAgAHAAcgBvAHAAZQByAHQAeQAgAGwAaQBiAHIAYQByAGkAZQBzAA0ACgBSAGUAYQBkAGkAbgBnACAAdABoAGUAcgBtAG8AZAB5AG4AYQBtAGkAYwAgAHAAcgBvAHAAZQByAHQAeQAgAG8AcAB0AGkAbwBuAHMADQAKAEsALQB2AGEAbAB1AGUAOgAgAEQARQBDAEgARQBNAEEADQAKAFIAZQBhAGQAaQBuAGcAIABwAGgAeQBzAGkAYwBhAGwAIABwAHIAbwBwAGUAcgB0AHkAIABvAHAAdABpAG8AbgBzAA0ACgBSAGUAYQBkAGkAbgBnACAAdABoAGUAcgBtAG8AZAB5AG4AYQBtAGkAYwAgAHAAcgBvAHAAZQByAHQAeQAgAGQAYQB0AGEADQAKAFcAYQByAG4AaQBuAGcAIQAhACAARQBzAHQAaQBtAGEAdABpAG4AZwAgAGEAYwB0AGkAdgBpAHQAeQAgAG0AbwBkAGUAbAAgAHAAYQByAGEAbQBlAHQAZQByAHMADQAKAFIAZQBhAGQAaQBuAGcAIAByAGUAYQBjAHQAaQBvAG4AIABkAGEAdABhAA0ACgBSAGUAYQBkAGkAbgBnACAAcwBwAGUAYwBpAGYAaQBjAGEAdABpAG8AbgBzAA0ACgBDAGgAZQBjAGsAaQBuAGcAIABjAG8AbQBwAG8AbgBlAG4AdABzACAAZABhAHQAYQAgACgAMwApAA0ACgBEAGUAdABlAHIAbQBpAG4AaQBuAGcAIABmAGUAZQBkACAAYwBvAG4AZABpAHQAaQBvAG4AcwANAAoAIABGAGUAZQBkAC0AZgBsAGEAcwBoACAAbwBuACAAcwB0AGEAZwBlACAAIAA0AA0ACgAgAEYAZQBlAGQALQBmAGwAYQBzAGgAIABvAG4AIABzAHQAYQBnAGUAIAAxADYADQAKAFIAZQBhAGQAaQBuAGcAIAAgACAAIAAgACAAIAA0ADQAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAUgB1AG4AIABsAGUAdgBlAGwAOgAgAEkAbgBpAHQAaQBhAGwAaQB6AGEAdABpAG8AbgAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAFIAZQBhAGQAaQBuAGcAIABpAG4AaQB0AGkAYQBsACAAdABlAG0AcABlAHIAYQB0AHUAcgBlACAAcAByAG8AZgBpAGwAZQBzAA0ACgBJAG4AaQB0AGkAYQBsAGkAegBpAG4AZwAgAGYAcgBvAG0AIABvAGwAZAAgAHIAZQBzAHUAbAB0AHMADQAKAFIAZQBhAGQAaQBuAGcAIABpAG4AaQB0AGkAYQBsACAAYwBvAG0AcABvAHMAaQB0AGkAbwBuACAAcAByAG8AZgBpAGwAZQBzAA0ACgBJAG4AaQB0AGkAYQBsAGkAegBhAHQAaQBvAG4AIAAgACAAIAAgACAAIAAgADAAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAUgB1AG4AIABsAGUAdgBlAGwAOgAgAEMAbwBtAHAAbABlAHQAZQAgAG0AbwBkAGUAbAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgAA0ACgANAAoAIAAgACAAIAAgACAASQB0AGUAcgBhAHQAaQBvAG4AIAAgACAAIABsAG8AZwAoAEUAcgByAC8AVABvAGwAKQANAAoAIAAgACAAIAAgACAAIAAgACAAMAAgACAAIAAgACAAIAAgACAAIAAgACAAMgAuADYANgAyADIADQAKACAAIAAgACAAIAAgACAAIAAgADEAIAAgACAAIAAgACAAIAAgACAAIAAgADMALgA3ADcAMAA1AA0ACgAgACAAIAAgACAAIAAgACAAIAAyACAAIAAgACAAIAAgACAAIAAgACAAIAAxAC4AOAA4ADMAMwANAAoAIAAgACAAIAAgACAAIAAgACAAMwAgACAAIAAgACAAIAAgACAAIAAgAC0AMQAuADkANAA1ADcADQAKAFMAaQBtAHUAbABhAHQAaQBvAG4AIAAgACAAIAAgACAAIAA0ADAAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAUgB1AG4AIABsAGUAdgBlAGwAOgAgAFIAZQBwAG8AcgB0ACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAEMAbwBuAHYAZQByAGcAZQBuAGMAZQAgAG8AYgB0AGEAaQBuAGUAZAAgAGkAbgAgADMAIABpAHQAZQByAGEAdABpAG8AbgBzACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAADQAKAFIAZQBwAG8AcgB0ACAAIAAgACAAIAAgACAAIAA5ACAAbQBpAGwAbABpAHMAZQBjAG8AbgBkAHMADQAKAEMAYQBwAGUALQBPAHAAZQBuACAAYwBsAGUAYQBuAHUAcAAgAGMAYQBsAGwAZQBkACAAdwBpAHQAaAAgAGMAbwBuAHYAZQByAGcAZQBkAA0ACgAgAEYAaQB4AE0AZQBtACAAZAByAGkAdgBlAHIAIABkAG8AbgBlAA0ACgANAAoAcgB1AG4AIAB0AGkAbQBlADoAIAAwAC4AMQA2ACAAcwBlAGMAbwBuAGQAcwANAAoAAADjAAAAVQBzAGkAbgBnADoAIABDADoAXABQAHIAbwBnAHIAYQBtACAARgBpAGwAZQBzAFwAQwBoAGUAbQBTAGUAcABMADgAdgA0ADAAXABiAGkAbgBcAGMAbwAtAGMAbwBsADIALgBlAHgAZQANAAoADQAKAEMAQQBQAEUALQBPAFAARQBOACAAdABoAGUAcgBtAG8ALQBwAHIAbwBwAGUAcgB0AGkAZQBzACAAdwBlAHIAZQAgAGQAaQBzAGEAYgBsAGUAZAAuAA0ACgBBAGwAbAAgAGMAYQBsAGMAdQBsAGEAdABpAG8AbgAgAG0AZQB0AGgAbwBkAHMAIABoAGEAdgBlACAAYgBlAGUAbgAgAGQAZQB0AGUAcgBtAGkAbgBlAGQAIABiAHkAIABDAGgAZQBtAFMAZQBwAC4ADQAKAFMAZQBlACAAbwB1AHQAcAB1AHQAIAByAGUAcABvAHIAdAAgAG8AcgAgAGcAcgBhAHAAaABpAGMAYQBsACAAdQBzAGUAcgAgAGkAbgB0AGUAcgBmAGEAYwBlACAAZgBvAHIAIABtAG8AcgBlACAAaQBuAGYAbwByAG0AYQB0AGkAbwBuAC4ADQAKAAAAAAAAAAAAAAAAAAAAAgAAABAAAAAAAKYCDQAAAEYAZQBlAGQAMQBfAHMAdABhAGcAZQAxADYABQAAAEYAZQBlAGQAMQAEAAAAZQBuAAwAA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</ParameterData>
</SimulationObject>
<SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
@@ -3018,18 +2670,18 @@ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
<OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
<FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mass</DefinedFlow>
+ <DefinedFlow>Mole</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-231.96284514096</TotalEnergyFlow>
+ <TotalEnergyFlow>-88.8133969332907</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</ComponentName>
- <Name2>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name2>
+ <ComponentName>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</ComponentName>
+ <Name2>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
<ReferenceSolvent></ReferenceSolvent>
- <SpecType>Pressure_and_Enthalpy</SpecType>
+ <SpecType>Temperature_and_Pressure</SpecType>
<CompositionBasis>Molar_Fractions</CompositionBasis>
<EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
<MobileCompatible>true</MobileCompatible>
@@ -3044,7 +2696,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:22</LastUpdated>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -3052,7 +2705,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name>
+ <Name>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -3078,19 +2731,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1.3476557234073E-14</MassFraction>
- <MoleFraction>1.77051224028859E-14</MoleFraction>
- <Molarity>1.74759365098677E-10</Molarity>
+ <MassFraction>2.96309664630914E-14</MassFraction>
+ <MoleFraction>9.6103846741447E-15</MoleFraction>
+ <Molarity>5.07491556858069E-10</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>37.7876156655895</Kvalue>
- <lnKvalue>3.63198142104934</lnKvalue>
- <MassFlow>1.15789859986823E-15</MassFlow>
- <MolarFlow>1.99365658628594E-14</MolarFlow>
+ <Kvalue>226.22247443778</Kvalue>
+ <lnKvalue>5.42151891523535</lnKvalue>
+ <MassFlow>2.04605812410343E-16</MassFlow>
+ <MolarFlow>3.52287951251245E-15</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>2.73334381070129E-18</VolumetricFlow>
+ <VolumetricFlow>5.01322547714005E-19</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -3103,19 +2756,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0686568094568745</MassFraction>
- <MoleFraction>0.290792198907833</MoleFraction>
- <Molarity>2870.28007490632</Molarity>
+ <MassFraction>0.94680617031014</MassFraction>
+ <MoleFraction>0.99</MoleFraction>
+ <Molarity>52278.5152025355</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.468971406767856</Kvalue>
- <lnKvalue>-0.757213478774221</lnKvalue>
- <MassFlow>0.00589895639967601</MassFlow>
- <MolarFlow>0.327441838243758</MolarFlow>
+ <Kvalue>0.980071004539983</Kvalue>
+ <lnKvalue>-0.0201302563299281</lnKvalue>
+ <MassFlow>0.00653782406701898</MassFlow>
+ <MolarFlow>0.362904382669544</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>1.09989655845932E-05</VolumetricFlow>
+ <VolumetricFlow>1.28447282569353E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -3128,19 +2781,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.931343190543112</MassFraction>
- <MoleFraction>0.709207801092149</MoleFraction>
- <Molarity>7000.27383158279</Molarity>
+ <MassFraction>0.0531938296898301</MassFraction>
+ <MoleFraction>0.0099999999999904</MoleFraction>
+ <Molarity>528.065810126115</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1.21773445254051</Kvalue>
- <lnKvalue>0.196992126257385</lnKvalue>
- <MassFlow>0.0800205095111489</MassFlow>
- <MolarFlow>0.798591939393914</MolarFlow>
+ <Kvalue>2.97297055032713</Kvalue>
+ <lnKvalue>1.0895616382579</lnKvalue>
+ <MassFlow>0.000367310555072917</MassFlow>
+ <MolarFlow>0.00366570083504238</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0.000217161234603844</VolumetricFlow>
+ <VolumetricFlow>1.03877173397222E-06</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -3156,29 +2809,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>753.150337700128</density>
- <enthalpy>0.137003835319227</enthalpy>
- <entropy>0.000459511493378659</entropy>
+ <density>994.725339664221</density>
+ <enthalpy>-51.6540257632069</enthalpy>
+ <entropy>-0.18093521066719</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0859194659108261</massflow>
- <massfraction>1</massfraction>
- <molar_enthalpy>10.4537684322914</molar_enthalpy>
- <molar_entropy>0.035061987371114</molar_entropy>
- <molarflow>1.12603377763769</molarflow>
- <molarfraction>1</molarfraction>
- <molecularWeight>76.3027429701769</molecularWeight>
+ <massflow>0.00690513462209211</massflow>
+ <molar_enthalpy>-973.0144867741</molar_enthalpy>
+ <molar_entropy>-3.4083031970008</molar_entropy>
+ <molarflow>0.36657008350459</molarflow>
+ <molecularWeight>18.8371471999996</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0346473655632416</surfaceTension>
- <temperature>298.151052353177</temperature>
- <thermalConductivity>0.127542517970083</thermalConductivity>
- <volumetric_flow>0.00011408010009422</volumetric_flow>
+ <surfaceTension>0.0735289992045926</surfaceTension>
+ <temperature>285.4835472473</temperature>
+ <thermalConductivity>0.538574741400444</thermalConductivity>
+ <volumetric_flow>6.94174999545402E-06</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.0671007250710113</helmholtz_energy>
- <internal_energy>0.069903110248216</internal_energy>
+ <helmholtz_energy>-0.111562161436453</helmholtz_energy>
+ <internal_energy>-51.7655879246434</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-5.11996937820588</molar_helmholtz_energy>
- <molar_internal_energy>5.33379905408556</molar_internal_energy>
+ <molar_helmholtz_energy>-2.10151285692858</molar_helmholtz_energy>
+ <molar_internal_energy>-975.115999631029</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -3190,20 +2841,20 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1.3476557234073E-14</MassFraction>
- <MoleFraction>1.77051224028859E-14</MoleFraction>
- <Molarity>1.74759365098677E-10</Molarity>
+ <MassFraction>2.96309664630914E-14</MassFraction>
+ <MoleFraction>9.6103846741447E-15</MoleFraction>
+ <Molarity>5.07491556858069E-10</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>1.15789859986823E-15</MassFlow>
- <MolarFlow>1.99365658628594E-14</MolarFlow>
+ <MassFlow>2.04605812410343E-16</MassFlow>
+ <MolarFlow>3.52287951251245E-15</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737985308993798</PartialVolume>
- <VolumetricFlow>1.36667190535064E-18</VolumetricFlow>
- <VolumetricFraction>1.19799325581052E-14</VolumetricFraction>
+ <PartialVolume>0.0724941600926307</PartialVolume>
+ <VolumetricFlow>2.50661273857003E-19</VolumetricFlow>
+ <VolumetricFraction>3.61092338417768E-14</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -3215,20 +2866,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0686568094568745</MassFraction>
- <MoleFraction>0.290792198907833</MoleFraction>
- <Molarity>2870.28007490632</Molarity>
+ <MassFraction>0.94680617031014</MassFraction>
+ <MoleFraction>0.99</MoleFraction>
+ <Molarity>52278.5152025355</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00589895639967601</MassFlow>
- <MolarFlow>0.327441838243758</MolarFlow>
+ <MassFlow>0.00653782406701898</MassFlow>
+ <MolarFlow>0.362904382669544</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.018080959744143</PartialVolume>
- <VolumetricFlow>5.4994827922966E-06</VolumetricFlow>
- <VolumetricFraction>0.0482072051808731</VolumetricFraction>
+ <PartialVolume>0.0180308533901994</PartialVolume>
+ <VolumetricFlow>6.42236412846766E-06</VolumetricFlow>
+ <VolumetricFraction>0.925179404714014</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -3240,20 +2891,20 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.931343190543112</MassFraction>
- <MoleFraction>0.709207801092149</MoleFraction>
- <Molarity>7000.27383158279</Molarity>
+ <MassFraction>0.0531938296898301</MassFraction>
+ <MoleFraction>0.0099999999999904</MoleFraction>
+ <Molarity>528.065810126115</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0800205095111489</MassFlow>
- <MolarFlow>0.798591939393914</MolarFlow>
+ <MassFlow>0.000367310555072917</MassFlow>
+ <MolarFlow>0.00366570083504238</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146373071297317</PartialVolume>
- <VolumetricFlow>0.000108580617301922</VolumetricFlow>
- <VolumetricFraction>0.951792794819115</VolumetricFraction>
+ <PartialVolume>0.144359935545783</PartialVolume>
+ <VolumetricFlow>5.1938586698611E-07</VolumetricFlow>
+ <VolumetricFraction>0.0748205952859499</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -3268,29 +2919,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00206548001295266</compressibilityFactor>
- <density>753.150337700128</density>
- <enthalpy>0.137003835319227</enthalpy>
- <entropy>0.000459511493378659</entropy>
+ <compressibilityFactor>0.000885402913570138</compressibilityFactor>
+ <density>994.725339664221</density>
+ <enthalpy>-51.6540257632069</enthalpy>
+ <entropy>-0.18093521066719</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>6.73620125558734E-07</kinematic_viscosity>
- <massflow>0.0859194659108261</massflow>
+ <kinematic_viscosity>1.2305065548107E-06</kinematic_viscosity>
+ <massflow>0.00690513462209211</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>10.4537684322914</molar_enthalpy>
- <molar_entropy>0.035061987371114</molar_entropy>
- <molarflow>1.12603377763769</molarflow>
+ <molar_enthalpy>-973.0144867741</molar_enthalpy>
+ <molar_entropy>-3.4083031970008</molar_entropy>
+ <molarflow>0.36657008350459</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>76.3027429701769</molecularWeight>
- <thermalConductivity>0.127542517970083</thermalConductivity>
- <viscosity>0.000507337225046163</viscosity>
- <volumetric_flow>0.00011408010009422</volumetric_flow>
+ <molecularWeight>18.8371471999996</molecularWeight>
+ <thermalConductivity>0.538574741400444</thermalConductivity>
+ <viscosity>0.00122401605069313</viscosity>
+ <volumetric_flow>6.94174999545402E-06</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.0671007250710113</helmholtz_energy>
- <internal_energy>0.069903110248216</internal_energy>
+ <helmholtz_energy>-0.111562161436453</helmholtz_energy>
+ <internal_energy>-51.7655879246434</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-5.11996937820588</molar_helmholtz_energy>
- <molar_internal_energy>5.33379905408556</molar_internal_energy>
+ <molar_helmholtz_energy>-2.10151285692858</molar_helmholtz_energy>
+ <molar_internal_energy>-975.115999631029</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -3302,8 +2953,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>4.36624604712041E-13</MassFraction>
- <MoleFraction>6.69034360672472E-13</MoleFraction>
+ <MassFraction>6.17190686337397E-12</MassFraction>
+ <MoleFraction>2.17408500128393E-12</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -3312,11 +2963,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>6.77899065951382E-08</PartialPressure>
- <PartialVolume>15.9657577978113</PartialVolume>
+ <PartialPressure>2.20289162755094E-07</PartialPressure>
+ <PartialVolume>66.4993401553277</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>4.0453203791847E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>3.74935198609097E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -3327,8 +2978,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0276063975567298</MassFraction>
- <MoleFraction>0.136373226598925</MoleFraction>
+ <MassFraction>0.85439051558988</MassFraction>
+ <MoleFraction>0.970270294494583</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -3337,11 +2988,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>13818.017185136</PartialPressure>
- <PartialVolume>4.95233912106403</PartialVolume>
+ <PartialPressure>98312.6375896636</PartialPressure>
+ <PartialVolume>20.6271000692068</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.16939262355314E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>2.01067301951728E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -3352,8 +3003,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.972393602442834</MassFraction>
- <MoleFraction>0.863626773400406</MoleFraction>
+ <MassFraction>0.145609484403948</MassFraction>
+ <MoleFraction>0.0297297055032428</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -3362,11 +3013,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>87506.9828147962</PartialPressure>
- <PartialVolume>27.5451885626456</PartialVolume>
+ <PartialPressure>3012.36241011608</PartialPressure>
+ <PartialVolume>114.729090035495</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>1.82574282659985E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>1.69216572517381E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -3395,23 +3046,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>8.34028837307649</ActivityCoeff>
+ <ActivityCoeff>19.1638009756031</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1.3476557234073E-14</MassFraction>
- <MoleFraction>1.77051224028859E-14</MoleFraction>
- <Molarity>1.74759365098677E-10</Molarity>
+ <MassFraction>2.96309664630914E-14</MassFraction>
+ <MoleFraction>9.6103846741447E-15</MoleFraction>
+ <Molarity>5.07491556858069E-10</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>2.52423158142427</FugacityCoeff>
+ <FugacityCoeff>3.26945040615609</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>1.15789859986823E-15</MassFlow>
- <MolarFlow>1.99365658628594E-14</MolarFlow>
+ <MassFlow>2.04605812410343E-16</MassFlow>
+ <MolarFlow>3.52287951251245E-15</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>1.79397152747242E-09</PartialPressure>
- <PartialVolume>0.0737985308993798</PartialVolume>
- <VolumetricFlow>1.36667190535064E-18</VolumetricFlow>
- <VolumetricFraction>1.19799325581052E-14</VolumetricFraction>
- <DiffusionCoefficient>3.54868780124732E-09</DiffusionCoefficient>
+ <PartialPressure>9.73772227107712E-10</PartialPressure>
+ <PartialVolume>0.0724941600926307</PartialVolume>
+ <VolumetricFlow>2.50661273857003E-19</VolumetricFlow>
+ <VolumetricFraction>3.61092338417768E-14</VolumetricFraction>
+ <DiffusionCoefficient>1.42353767023296E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -3420,23 +3071,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00071618663116</ActivityCoeff>
+ <ActivityCoeff>1.00075912901874</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0686568094568745</MassFraction>
- <MoleFraction>0.290792198907833</MoleFraction>
- <Molarity>2870.28007490632</Molarity>
+ <MassFraction>0.94680617031014</MassFraction>
+ <MoleFraction>0.99</MoleFraction>
+ <Molarity>52278.5152025355</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0313453774702483</FugacityCoeff>
+ <FugacityCoeff>0.014164900852859</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00589895639967601</MassFlow>
- <MolarFlow>0.327441838243758</MolarFlow>
+ <MassFlow>0.00653782406701898</MassFlow>
+ <MolarFlow>0.362904382669544</MolarFlow>
<Name>Water</Name>
- <PartialPressure>29464.5195543362</PartialPressure>
- <PartialVolume>0.018080959744143</PartialVolume>
- <VolumetricFlow>5.4994827922966E-06</VolumetricFlow>
- <VolumetricFraction>0.0482072051808731</VolumetricFraction>
- <DiffusionCoefficient>4.5959358233994E-09</DiffusionCoefficient>
+ <PartialPressure>100311.75</PartialPressure>
+ <PartialVolume>0.0180308533901994</PartialVolume>
+ <VolumetricFlow>6.42236412846766E-06</VolumetricFlow>
+ <VolumetricFraction>0.925179404714014</VolumetricFraction>
+ <DiffusionCoefficient>1.82705418789284E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -3445,23 +3096,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.00551400815334</ActivityCoeff>
+ <ActivityCoeff>1.00591690972668</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.931343190543112</MassFraction>
- <MoleFraction>0.709207801092149</MoleFraction>
- <Molarity>7000.27383158279</Molarity>
+ <MassFraction>0.0531938296898301</MassFraction>
+ <MoleFraction>0.0099999999999904</MoleFraction>
+ <Molarity>528.065810126115</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0813916275546046</FugacityCoeff>
+ <FugacityCoeff>0.0429681450515103</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0800205095111489</MassFlow>
- <MolarFlow>0.798591939393914</MolarFlow>
+ <MassFlow>0.000367310555072917</MassFlow>
+ <MolarFlow>0.00366570083504238</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>71860.480445662</PartialPressure>
- <PartialVolume>0.146373071297317</PartialVolume>
- <VolumetricFlow>0.000108580617301922</VolumetricFlow>
- <VolumetricFraction>0.951792794819115</VolumetricFraction>
- <DiffusionCoefficient>3.09063571282714E-09</DiffusionCoefficient>
+ <PartialPressure>1013.24999999903</PartialPressure>
+ <PartialVolume>0.144359935545783</PartialVolume>
+ <VolumetricFlow>5.1938586698611E-07</VolumetricFlow>
+ <VolumetricFraction>0.0748205952859499</VolumetricFraction>
+ <DiffusionCoefficient>1.23683246545162E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -3475,36 +3126,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00206548001295266</compressibilityFactor>
- <density>753.150337700128</density>
- <enthalpy>0.137003835319227</enthalpy>
- <enthalpyF>-2699.77056633137</enthalpyF>
- <entropy>0.000459511493378659</entropy>
- <entropyF>0.00045951149316539</entropyF>
+ <compressibilityFactor>0.000885402913570138</compressibilityFactor>
+ <density>994.725339664221</density>
+ <enthalpy>-51.6540257632069</enthalpy>
+ <enthalpyF>-12861.935616598</enthalpyF>
+ <entropy>-0.18093521066719</entropy>
+ <entropyF>-0.180935210667659</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>6.73620125558734E-07</kinematic_viscosity>
- <massflow>0.0859194659108261</massflow>
+ <kinematic_viscosity>1.2305065548107E-06</kinematic_viscosity>
+ <massflow>0.00690513462209211</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>10.4537684322914</molar_enthalpy>
- <molar_entropy>0.035061987371114</molar_entropy>
- <molarflow>1.12603377763769</molarflow>
+ <molar_enthalpy>-973.0144867741</molar_enthalpy>
+ <molar_entropy>-3.4083031970008</molar_entropy>
+ <molarflow>0.36657008350459</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>76.3027429701769</molecularWeight>
+ <molecularWeight>18.8371471999996</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.127542517970083</thermalConductivity>
- <viscosity>0.000507337225046163</viscosity>
- <volumetric_flow>0.00011408010009422</volumetric_flow>
- <bulk_modulus>-99.4074478736877</bulk_modulus>
+ <thermalConductivity>0.538574741400444</thermalConductivity>
+ <viscosity>0.00122401605069313</viscosity>
+ <volumetric_flow>6.94174999545402E-06</volumetric_flow>
+ <bulk_modulus>1149.00631291247</bulk_modulus>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.0671007250710113</helmholtz_energy>
- <internal_energy>0.069903110248216</internal_energy>
- <isothermal_compressibility>-0.0100596084236128</isothermal_compressibility>
+ <helmholtz_energy>-0.111562161436453</helmholtz_energy>
+ <internal_energy>-51.7655879246434</internal_energy>
+ <isothermal_compressibility>0.000870317237392048</isothermal_compressibility>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-5.11996937820588</molar_helmholtz_energy>
- <molar_internal_energy>5.33379905408556</molar_internal_energy>
- <idealGasHeatCapacityCp>1.64867209641396</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.07076696077004</idealGasHeatCapacityRatio>
+ <molar_helmholtz_energy>-2.10151285692858</molar_helmholtz_energy>
+ <molar_internal_energy>-975.115999631029</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.84749766625772</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.31388289441633</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -3527,7 +3178,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0737985308993798</PartialVolume>
+ <PartialVolume>0.0724941600926307</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3552,7 +3203,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.018080959744143</PartialVolume>
+ <PartialVolume>0.0180308533901994</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3577,7 +3228,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.146373071297317</PartialVolume>
+ <PartialVolume>0.144359935545783</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3611,8 +3262,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -3622,7 +3271,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737985308993798</PartialVolume>
+ <PartialVolume>0.0724941600926307</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3636,8 +3285,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -3647,7 +3294,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.018080959744143</PartialVolume>
+ <PartialVolume>0.0180308533901994</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3661,8 +3308,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -3672,7 +3317,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146373071297317</PartialVolume>
+ <PartialVolume>0.144359935545783</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3706,8 +3351,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -3717,7 +3360,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737985308993798</PartialVolume>
+ <PartialVolume>0.0724941600926307</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3731,8 +3374,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -3742,7 +3383,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.018080959744143</PartialVolume>
+ <PartialVolume>0.0180308533901994</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3756,8 +3397,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -3767,7 +3406,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146373071297317</PartialVolume>
+ <PartialVolume>0.144359935545783</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3812,7 +3451,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737985308993798</PartialVolume>
+ <PartialVolume>0.0724941600926307</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3837,7 +3476,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.018080959744143</PartialVolume>
+ <PartialVolume>0.0180308533901994</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3862,7 +3501,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146373071297317</PartialVolume>
+ <PartialVolume>0.144359935545783</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -3898,7 +3537,7 @@ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
<DefinedFlow>Mole</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-315.967185386889</TotalEnergyFlow>
+ <TotalEnergyFlow>-315.622386454292</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
<ComponentName>MAT-03b2c90d-8474-4909-bef0-39eb7b0a6f41</ComponentName>
@@ -3922,7 +3561,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:26</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:59</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -3956,19 +3596,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.196081529098452</MassFraction>
- <MoleFraction>0.23395179015531</MoleFraction>
- <Molarity>2496.34184254518</Molarity>
+ <MassFraction>0.196310640176173</MassFraction>
+ <MoleFraction>0.23421188262113</MoleFraction>
+ <Molarity>2499.28455305808</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>3.12751219819409</Kvalue>
- <lnKvalue>1.14023786365319</lnKvalue>
- <MassFlow>0.0212014158783692</MassFlow>
- <MolarFlow>0.365043557435066</MolarFlow>
+ <Kvalue>3.12442569994755</Kvalue>
+ <lnKvalue>1.1392504902827</lnKvalue>
+ <MassFlow>0.0212014158175207</MassFlow>
+ <MolarFlow>0.365043556387382</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>-8.29414615119851E-05</VolumetricFlow>
+ <VolumetricFlow>-8.29982110214932E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -3981,19 +3621,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0665889936708942</MassFraction>
- <MoleFraction>0.25613639917885</MoleFraction>
- <Molarity>2733.05885047748</Molarity>
+ <MassFraction>0.0665705258123249</MassFraction>
+ <MoleFraction>0.25605085683547</MoleFraction>
+ <Molarity>2732.32913772088</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.246281963317467</Kvalue>
- <lnKvalue>-1.40127820707929</lnKvalue>
- <MassFlow>0.00719996908546073</MassFlow>
- <MolarFlow>0.399659016427207</MolarFlow>
+ <Kvalue>0.246278525815052</Kvalue>
+ <lnKvalue>-1.40129216476567</lnKvalue>
+ <MassFlow>0.00718957157733013</MassFlow>
+ <MolarFlow>0.399081867022335</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>2.13514913383788E-05</VolumetricFlow>
+ <VolumetricFlow>2.13353950968869E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -4006,19 +3646,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.737329477230654</MassFraction>
- <MoleFraction>0.50991181066585</MoleFraction>
- <Molarity>5440.92519287033</Molarity>
+ <MassFraction>0.737118834011502</MassFraction>
+ <MoleFraction>0.5097372605434</MoleFraction>
+ <Molarity>5439.42709967067</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.402483611754566</Kvalue>
- <lnKvalue>-0.910100899090169</lnKvalue>
- <MassFlow>0.0797241278055245</MassFlow>
- <MolarFlow>0.795634097178943</MolarFlow>
+ <Kvalue>0.402486855545172</Kvalue>
+ <lnKvalue>-0.910092839687399</lnKvalue>
+ <MassFlow>0.0796083334697449</MassFlow>
+ <MolarFlow>0.794478488151383</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0.000354052766104535</VolumetricFlow>
+ <VolumetricFlow>0.000353781259133261</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -4034,27 +3674,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>739.413793984863</density>
- <enthalpy>107.694538182394</enthalpy>
- <entropy>0.322240863236603</entropy>
+ <density>739.421446166298</density>
+ <enthalpy>107.673458458026</enthalpy>
+ <entropy>0.32218374822565</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.108125512769354</massflow>
- <molar_enthalpy>7462.82990045978</molar_enthalpy>
- <molar_entropy>22.3300901781966</molar_entropy>
- <molarflow>1.5603366710412</molarflow>
- <molecularWeight>69.2962709754191</molecularWeight>
+ <massflow>0.107999320864596</massflow>
+ <molar_enthalpy>7460.94649343064</molar_enthalpy>
+ <molar_entropy>22.3248676228002</molar_entropy>
+ <molarflow>1.5586039115611</molarflow>
+ <molecularWeight>69.2923455815168</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0293667055648529</surfaceTension>
- <temperature>334.205094601301</temperature>
- <thermalConductivity>0.124488729483069</thermalConductivity>
- <volumetric_flow>0.000146231397965465</volumetric_flow>
- <gibbs_free_energy>-1.42108547152019E-14</gibbs_free_energy>
- <helmholtz_energy>-0.079003966941925</helmholtz_energy>
- <internal_energy>107.615534215452</internal_energy>
- <molar_gibbs_free_energy>-9.84759239136941E-13</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-5.47468030134069</molar_helmholtz_energy>
- <molar_internal_energy>7457.35522015844</molar_internal_energy>
+ <surfaceTension>0.0293638785553052</surfaceTension>
+ <temperature>334.198913045775</temperature>
+ <thermalConductivity>0.124495817680915</thermalConductivity>
+ <volumetric_flow>0.000146059221604328</volumetric_flow>
+ <gibbs_free_energy>-1.4210854715202E-14</gibbs_free_energy>
+ <helmholtz_energy>-0.0790179063344425</helmholtz_energy>
+ <internal_energy>107.594440551692</internal_energy>
+ <molar_gibbs_free_energy>-9.84703455934505E-13</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-5.47533607285412</molar_helmholtz_energy>
+ <molar_internal_energy>7455.47115735778</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -4066,20 +3706,20 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.196081529098452</MassFraction>
- <MoleFraction>0.233951790155308</MoleFraction>
- <Molarity>2496.34184254516</Molarity>
+ <MassFraction>0.196310640176173</MassFraction>
+ <MoleFraction>0.23421188262113</MoleFraction>
+ <Molarity>2499.28455305808</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.021201415878369</MassFlow>
- <MolarFlow>0.365043557435062</MolarFlow>
+ <MassFlow>0.0212014158175207</MassFlow>
+ <MolarFlow>0.365043556387382</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0780058205985097</PartialVolume>
- <VolumetricFlow>-4.14707307559925E-05</VolumetricFlow>
- <VolumetricFraction>-0.28359662379612</VolumetricFraction>
+ <PartialVolume>-0.0780050254443918</PartialVolume>
+ <VolumetricFlow>-4.14991055107466E-05</VolumetricFlow>
+ <VolumetricFraction>-0.28412519973006</VolumetricFraction>
<DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -4091,20 +3731,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0665889936708942</MassFraction>
- <MoleFraction>0.256136399178847</MoleFraction>
- <Molarity>2733.05885047745</Molarity>
+ <MassFraction>0.0665705258123249</MassFraction>
+ <MoleFraction>0.25605085683547</MoleFraction>
+ <Molarity>2732.32913772088</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00719996908546066</MassFlow>
- <MolarFlow>0.399659016427203</MolarFlow>
+ <MassFlow>0.00718957157733013</MassFlow>
+ <MolarFlow>0.399081867022335</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183416589386652</PartialVolume>
- <VolumetricFlow>1.06757456691894E-05</VolumetricFlow>
- <VolumetricFraction>0.0730058374447785</VolumetricFraction>
+ <PartialVolume>0.0183416006167318</PartialVolume>
+ <VolumetricFlow>1.06676975484434E-05</VolumetricFlow>
+ <VolumetricFraction>0.0730367958371165</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -4116,20 +3756,20 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.737329477230654</MassFraction>
- <MoleFraction>0.509911810665845</MoleFraction>
- <Molarity>5440.92519287028</Molarity>
+ <MassFraction>0.737118834011502</MassFraction>
+ <MoleFraction>0.5097372605434</MoleFraction>
+ <Molarity>5439.42709967067</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0797241278055237</MassFlow>
- <MolarFlow>0.795634097178935</MolarFlow>
+ <MassFlow>0.0796083334697449</MassFlow>
+ <MolarFlow>0.794478488151383</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152775818520635</PartialVolume>
- <VolumetricFlow>0.000177026383052268</VolumetricFlow>
- <VolumetricFraction>1.21059078635134</VolumetricFraction>
+ <PartialVolume>0.152774622413144</PartialVolume>
+ <VolumetricFlow>0.000176890629566631</VolumetricFlow>
+ <VolumetricFraction>1.21108840389294</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -4144,29 +3784,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00197031506116069</compressibilityFactor>
- <density>739.413793984855</density>
- <enthalpy>107.694538182395</enthalpy>
- <entropy>0.322240863236606</entropy>
+ <compressibilityFactor>0.0019705875192129</compressibilityFactor>
+ <density>739.421446166298</density>
+ <enthalpy>107.673458458026</enthalpy>
+ <entropy>0.32218374822565</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>3.96481141317246E-07</kinematic_viscosity>
- <massflow>0.108125512769353</massflow>
- <massfraction>0.99999999999999</massfraction>
- <molar_enthalpy>7462.82990045978</molar_enthalpy>
- <molar_entropy>22.3300901781966</molar_entropy>
- <molarflow>1.5603366710412</molarflow>
+ <kinematic_viscosity>3.96474450616239E-07</kinematic_viscosity>
+ <massflow>0.107999320864596</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>7460.94649343064</molar_enthalpy>
+ <molar_entropy>22.3248676228002</molar_entropy>
+ <molarflow>1.5586039115611</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>69.2962709754184</molecularWeight>
- <thermalConductivity>0.124488729483069</thermalConductivity>
- <viscosity>0.00029316362494483</viscosity>
- <volumetric_flow>0.000146231397965465</volumetric_flow>
+ <molecularWeight>69.2923455815168</molecularWeight>
+ <thermalConductivity>0.124495817680915</thermalConductivity>
+ <viscosity>0.000293161711642648</viscosity>
+ <volumetric_flow>0.000146059221604328</volumetric_flow>
<gibbs_free_energy>-1.4210854715202E-14</gibbs_free_energy>
- <helmholtz_energy>-0.0790039669419258</helmholtz_energy>
- <internal_energy>107.615534215453</internal_energy>
- <molar_gibbs_free_energy>-9.84759239136941E-13</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-5.47468030134069</molar_helmholtz_energy>
- <molar_internal_energy>7457.35522015844</molar_internal_energy>
+ <helmholtz_energy>-0.0790179063344425</helmholtz_energy>
+ <internal_energy>107.594440551692</internal_energy>
+ <molar_gibbs_free_energy>-9.84703455934505E-13</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-5.47533607285412</molar_helmholtz_energy>
+ <molar_internal_energy>7455.47115735778</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -4178,8 +3818,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.661961038431111</MassFraction>
- <MoleFraction>0.731687077500068</MoleFraction>
+ <MassFraction>0.662063690007847</MassFraction>
+ <MoleFraction>0.731777625294556</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -4189,10 +3829,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>24.8092432542014</PartialVolume>
+ <PartialVolume>24.8095612865622</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>4.93983202433397E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>4.93967213042265E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -4203,8 +3843,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0177023853370038</MassFraction>
- <MoleFraction>0.0630817752668329</MoleFraction>
+ <MassFraction>0.0176967804134546</MassFraction>
+ <MoleFraction>0.0630598275551205</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -4214,10 +3854,10 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>7.69545595565894</PartialVolume>
+ <PartialVolume>7.69555460453749</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.64909429926079E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>2.64900855261053E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -4228,8 +3868,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.320336576231885</MassFraction>
- <MoleFraction>0.205231147233099</MoleFraction>
+ <MassFraction>0.320239529578699</MassFraction>
+ <MoleFraction>0.205162547150323</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -4239,10 +3879,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>42.8025585874289</PartialVolume>
+ <PartialVolume>42.8031072780365</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.22945577547893E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>2.22938361180974E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -4271,22 +3911,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>2.65070108492138</ActivityCoeff>
+ <ActivityCoeff>2.64862668825502</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.196081529098452</MassFraction>
- <MoleFraction>0.233951790155308</MoleFraction>
- <Molarity>2496.34184254516</Molarity>
+ <MassFraction>0.196310640176173</MassFraction>
+ <MoleFraction>0.23421188262113</MoleFraction>
+ <Molarity>2499.28455305808</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>3.12759813607155</FugacityCoeff>
+ <FugacityCoeff>3.12451129325159</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.021201415878369</MassFlow>
- <MolarFlow>0.365043557435062</MolarFlow>
+ <MassFlow>0.0212014158175207</MassFlow>
+ <MolarFlow>0.365043556387382</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>23705.1651374865</PartialPressure>
- <PartialVolume>-0.0780058205985097</PartialVolume>
- <VolumetricFlow>-4.14707307559925E-05</VolumetricFlow>
- <VolumetricFraction>-0.28359662379612</VolumetricFraction>
+ <PartialPressure>23731.519006586</PartialPressure>
+ <PartialVolume>-0.0780050254443918</PartialVolume>
+ <VolumetricFlow>-4.14991055107466E-05</VolumetricFlow>
+ <VolumetricFraction>-0.28412519973006</VolumetricFraction>
<DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -4296,23 +3936,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.19031423519705</ActivityCoeff>
+ <ActivityCoeff>1.190635417056</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0665889936708942</MassFraction>
- <MoleFraction>0.256136399178847</MoleFraction>
- <Molarity>2733.05885047745</Molarity>
+ <MassFraction>0.0665705258123249</MassFraction>
+ <MoleFraction>0.25605085683547</MoleFraction>
+ <Molarity>2732.32913772088</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.246288730660916</FugacityCoeff>
+ <FugacityCoeff>0.246285272588624</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00719996908546066</MassFlow>
- <MolarFlow>0.399659016427203</MolarFlow>
+ <MassFlow>0.00718957157733013</MassFlow>
+ <MolarFlow>0.399081867022335</MolarFlow>
<Name>Water</Name>
- <PartialPressure>25953.0206467967</PartialPressure>
- <PartialVolume>0.0183416589386652</PartialVolume>
- <VolumetricFlow>1.06757456691894E-05</VolumetricFlow>
- <VolumetricFraction>0.0730058374447785</VolumetricFraction>
- <DiffusionCoefficient>8.83907951129381E-09</DiffusionCoefficient>
+ <PartialPressure>25944.353068854</PartialPressure>
+ <PartialVolume>0.0183416006167318</PartialVolume>
+ <VolumetricFlow>1.06676975484434E-05</VolumetricFlow>
+ <VolumetricFraction>0.0730367958371165</VolumetricFraction>
+ <DiffusionCoefficient>8.83899057122706E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -4321,23 +3961,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.10245721035157</ActivityCoeff>
+ <ActivityCoeff>1.10271424607101</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.737329477230654</MassFraction>
- <MoleFraction>0.509911810665845</MoleFraction>
- <Molarity>5440.92519287028</Molarity>
+ <MassFraction>0.737118834011502</MassFraction>
+ <MoleFraction>0.5097372605434</MoleFraction>
+ <Molarity>5439.42709967067</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.402494671211769</FugacityCoeff>
+ <FugacityCoeff>0.402497881629038</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0797241278055237</MassFlow>
- <MolarFlow>0.795634097178935</MolarFlow>
+ <MassFlow>0.0796083334697449</MassFlow>
+ <MolarFlow>0.794478488151383</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>51666.8142157167</PartialPressure>
- <PartialVolume>0.152775818520635</PartialVolume>
- <VolumetricFlow>0.000177026383052268</VolumetricFlow>
- <VolumetricFraction>1.21059078635134</VolumetricFraction>
- <DiffusionCoefficient>5.84325882884499E-09</DiffusionCoefficient>
+ <PartialPressure>51649.12792456</PartialPressure>
+ <PartialVolume>0.152774622413144</PartialVolume>
+ <VolumetricFlow>0.000176890629566631</VolumetricFlow>
+ <VolumetricFraction>1.21108840389294</VolumetricFraction>
+ <DiffusionCoefficient>5.84321633373963E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -4351,36 +3991,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00197031506116069</compressibilityFactor>
- <density>739.413793984855</density>
- <enthalpy>107.694538182395</enthalpy>
- <enthalpyF>-2922.22600655673</enthalpyF>
- <entropy>0.322240863236606</entropy>
- <entropyF>-2.78079035164359</entropyF>
+ <compressibilityFactor>0.0019705875192129</compressibilityFactor>
+ <density>739.421446166298</density>
+ <enthalpy>107.673458458026</enthalpy>
+ <enthalpyF>-2922.44788140848</enthalpyF>
+ <entropy>0.32218374822565</entropy>
+ <entropyF>-2.78447319738559</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>3.96481141317246E-07</kinematic_viscosity>
- <massflow>0.108125512769353</massflow>
- <massfraction>0.99999999999999</massfraction>
- <molar_enthalpy>7462.82990045978</molar_enthalpy>
- <molar_entropy>22.3300901781966</molar_entropy>
- <molarflow>1.5603366710412</molarflow>
+ <kinematic_viscosity>3.96474450616239E-07</kinematic_viscosity>
+ <massflow>0.107999320864596</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>7460.94649343064</molar_enthalpy>
+ <molar_entropy>22.3248676228002</molar_entropy>
+ <molarflow>1.5586039115611</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>69.2962709754184</molecularWeight>
+ <molecularWeight>69.2923455815168</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.124488729483069</thermalConductivity>
- <viscosity>0.00029316362494483</viscosity>
- <volumetric_flow>0.000146231397965465</volumetric_flow>
- <bulk_modulus>-136.008521221243</bulk_modulus>
+ <thermalConductivity>0.124495817680915</thermalConductivity>
+ <viscosity>0.000293161711642648</viscosity>
+ <volumetric_flow>0.000146059221604328</volumetric_flow>
+ <bulk_modulus>-136.068528604452</bulk_modulus>
<gibbs_free_energy>-1.4210854715202E-14</gibbs_free_energy>
- <helmholtz_energy>-0.0790039669419258</helmholtz_energy>
- <internal_energy>107.615534215453</internal_energy>
- <isothermal_compressibility>-0.00735248049916899</isothermal_compressibility>
- <molar_gibbs_free_energy>-9.84759239136941E-13</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-5.47468030134069</molar_helmholtz_energy>
- <molar_internal_energy>7457.35522015844</molar_internal_energy>
- <idealGasHeatCapacityCp>1.73156838233754</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.07444668768553</idealGasHeatCapacityRatio>
+ <helmholtz_energy>-0.0790179063344425</helmholtz_energy>
+ <internal_energy>107.594440551692</internal_energy>
+ <isothermal_compressibility>-0.00734923799247495</isothermal_compressibility>
+ <molar_gibbs_free_energy>-9.84703455934505E-13</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-5.47533607285412</molar_helmholtz_energy>
+ <molar_internal_energy>7455.47115735778</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.73144564312707</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.07445688974287</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -4403,7 +4043,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0780058205985097</PartialVolume>
+ <PartialVolume>-0.0780050254443918</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>NaN</DiffusionCoefficient>
@@ -4428,7 +4068,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183416589386652</PartialVolume>
+ <PartialVolume>0.0183416006167318</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4453,7 +4093,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152775818520635</PartialVolume>
+ <PartialVolume>0.152774622413144</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4487,8 +4127,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -4498,7 +4136,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0780058205985097</PartialVolume>
+ <PartialVolume>-0.0780050254443918</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>NaN</DiffusionCoefficient>
@@ -4512,8 +4150,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -4523,7 +4159,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183416589386652</PartialVolume>
+ <PartialVolume>0.0183416006167318</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4537,8 +4173,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -4548,7 +4182,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152775818520635</PartialVolume>
+ <PartialVolume>0.152774622413144</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4582,8 +4216,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -4593,7 +4225,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0780058205985097</PartialVolume>
+ <PartialVolume>-0.0780050254443918</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>NaN</DiffusionCoefficient>
@@ -4607,8 +4239,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -4618,7 +4248,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183416589386652</PartialVolume>
+ <PartialVolume>0.0183416006167318</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4632,8 +4262,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -4643,7 +4271,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152775818520635</PartialVolume>
+ <PartialVolume>0.152774622413144</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4688,7 +4316,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0780058205985097</PartialVolume>
+ <PartialVolume>-0.0780050254443918</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>NaN</DiffusionCoefficient>
@@ -4713,7 +4341,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183416589386652</PartialVolume>
+ <PartialVolume>0.0183416006167318</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4738,7 +4366,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.152775818520635</PartialVolume>
+ <PartialVolume>0.152774622413144</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -4772,18 +4400,18 @@ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
<OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
<FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mole</DefinedFlow>
+ <DefinedFlow>Mass</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-71.6632443919596</TotalEnergyFlow>
+ <TotalEnergyFlow>-248.683405184637</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</ComponentName>
- <Name2>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name2>
+ <ComponentName>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</ComponentName>
+ <Name2>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
<ReferenceSolvent></ReferenceSolvent>
- <SpecType>Temperature_and_Pressure</SpecType>
+ <SpecType>Pressure_and_Enthalpy</SpecType>
<CompositionBasis>Molar_Fractions</CompositionBasis>
<EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
<MobileCompatible>true</MobileCompatible>
@@ -4798,7 +4426,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:30</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:55</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -4806,7 +4435,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name>
+ <Name>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -4832,19 +4461,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.89784817887196E-14</MassFraction>
- <MoleFraction>9.3987605031104E-15</MoleFraction>
- <Molarity>4.96316408068559E-10</Molarity>
+ <MassFraction>5.53019096224656E-17</MassFraction>
+ <MoleFraction>6.94179247569153E-17</MoleFraction>
+ <Molarity>7.27489393760675E-13</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>226.222483899873</Kvalue>
- <lnKvalue>5.42151895706184</lnKvalue>
- <MassFlow>1.61460302974089E-16</MassFlow>
- <MolarFlow>2.78000505816871E-15</MolarFlow>
+ <Kvalue>39.9822446841827</Kvalue>
+ <lnKvalue>3.68843547267333</lnKvalue>
+ <MassFlow>4.81827165548904E-18</MassFlow>
+ <MolarFlow>8.2960451127359E-17</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>3.95607960637362E-19</VolumetricFlow>
+ <VolumetricFlow>1.12605052670969E-20</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -4857,19 +4486,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.94680617031014</MassFraction>
- <MoleFraction>0.99</MoleFraction>
- <Molarity>52278.5152175403</Molarity>
+ <MassFraction>0.082076281663556</MassFraction>
+ <MoleFraction>0.332145468660139</MoleFraction>
+ <Molarity>3480.83447441072</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.980071003951505</Kvalue>
- <lnKvalue>-0.0201302569303723</lnKvalue>
- <MassFlow>0.00527534921361959</MassFlow>
- <MolarFlow>0.292826379252479</MolarFlow>
+ <Kvalue>0.483957703480762</Kvalue>
+ <lnKvalue>-0.725757765586748</lnKvalue>
+ <MassFlow>0.00715103373874805</MassFlow>
+ <MolarFlow>0.39694269191198</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>1.03643699351317E-05</VolumetricFlow>
+ <VolumetricFlow>1.32004342676981E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -4882,19 +4511,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0531938296898311</MassFraction>
- <MoleFraction>0.0099999999999906</MoleFraction>
- <Molarity>528.065810277688</Molarity>
+ <MassFraction>0.917923718336444</MassFraction>
+ <MoleFraction>0.667854531339861</MoleFraction>
+ <Molarity>6999.0148772973</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>2.97297060859117</Kvalue>
- <lnKvalue>1.08956165785582</lnKvalue>
- <MassFlow>0.000296381705594235</MassFlow>
- <MolarFlow>0.00295784221466872</MolarFlow>
+ <Kvalue>1.25664437745442</Kvalue>
+ <lnKvalue>0.228444975860843</lnKvalue>
+ <MassFlow>0.0799756439543436</MassFlow>
+ <MolarFlow>0.798144188283104</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>8.38181554097333E-07</VolumetricFlow>
+ <VolumetricFlow>0.000214872859553135</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -4910,27 +4539,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>994.725339949722</density>
- <enthalpy>-51.6540322281299</enthalpy>
- <entropy>-0.18093523431587</entropy>
+ <density>764.023496425106</density>
+ <enthalpy>0.135692785336217</enthalpy>
+ <entropy>0.000455113855428359</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.00557173091921399</massflow>
- <molar_enthalpy>-973.014608554806</molar_enthalpy>
- <molar_entropy>-3.40830364247446</molar_entropy>
- <molarflow>0.29578422146715</molarflow>
- <molecularWeight>18.8371471999996</molecularWeight>
+ <massflow>0.0871266776930916</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>9.89255406379874</molar_enthalpy>
+ <molar_entropy>0.0331796448046473</molar_entropy>
+ <molarflow>1.19508688019508</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>72.9040533679604</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0735289994526015</surfaceTension>
- <temperature>285.48354566449</temperature>
- <thermalConductivity>0.538574739113174</thermalConductivity>
- <volumetric_flow>5.6012757446147E-06</volumetric_flow>
+ <surfaceTension>0.0368291121506369</surfaceTension>
+ <temperature>298.151294929268</temperature>
+ <thermalConductivity>0.129670963284751</thermalConductivity>
+ <volumetric_flow>0.000114036646910416</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.111562161263905</helmholtz_energy>
- <internal_energy>-51.7655943893938</internal_energy>
+ <helmholtz_energy>-0.064452667818253</helmholtz_energy>
+ <internal_energy>0.0712401175179639</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-2.10151285367827</molar_helmholtz_energy>
- <molar_internal_energy>-975.116121408485</molar_internal_energy>
+ <molar_helmholtz_energy>-4.69886073432934</molar_helmholtz_energy>
+ <molar_internal_energy>5.19369332946941</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -4942,20 +4573,20 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.89784817887196E-14</MassFraction>
- <MoleFraction>9.3987605031104E-15</MoleFraction>
- <Molarity>4.96316408068559E-10</Molarity>
+ <MassFraction>5.53019096224656E-17</MassFraction>
+ <MoleFraction>6.94179247569153E-17</MoleFraction>
+ <Molarity>7.27489393760675E-13</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>1.61460302974089E-16</MassFlow>
- <MolarFlow>2.78000505816871E-15</MolarFlow>
+ <MassFlow>4.81827165548904E-18</MassFlow>
+ <MolarFlow>8.2960451127359E-17</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0724941596865831</PartialVolume>
- <VolumetricFlow>1.97803980318681E-19</VolumetricFlow>
- <VolumetricFraction>3.53140943844548E-14</VolumetricFraction>
+ <PartialVolume>0.0737985565649378</PartialVolume>
+ <VolumetricFlow>5.63025263354846E-21</VolumetricFlow>
+ <VolumetricFraction>4.9372309569672E-17</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -4967,20 +4598,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.94680617031014</MassFraction>
- <MoleFraction>0.99</MoleFraction>
- <Molarity>52278.5152175403</Molarity>
+ <MassFraction>0.082076281663556</MassFraction>
+ <MoleFraction>0.332145468660139</MoleFraction>
+ <Molarity>3480.83447441072</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00527534921361959</MassFlow>
- <MolarFlow>0.292826379252479</MolarFlow>
+ <MassFlow>0.00715103373874805</MassFlow>
+ <MolarFlow>0.39694269191198</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180308538169985</PartialVolume>
- <VolumetricFlow>5.18218496756583E-06</VolumetricFlow>
- <VolumetricFraction>0.925179406235839</VolumetricFraction>
+ <PartialVolume>0.0180809607203663</PartialVolume>
+ <VolumetricFlow>6.60021713384904E-06</VolumetricFlow>
+ <VolumetricFraction>0.0578780358127679</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -4992,20 +4623,20 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0531938296898311</MassFraction>
- <MoleFraction>0.0099999999999906</MoleFraction>
- <Molarity>528.065810277688</Molarity>
+ <MassFraction>0.917923718336444</MassFraction>
+ <MoleFraction>0.667854531339861</MoleFraction>
+ <Molarity>6999.0148772973</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.000296381705594235</MassFlow>
- <MolarFlow>0.00295784221466872</MolarFlow>
+ <MassFlow>0.0799756439543436</MassFlow>
+ <MolarFlow>0.798144188283104</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.144359935789163</PartialVolume>
- <VolumetricFlow>4.19090777048666E-07</VolumetricFlow>
- <VolumetricFraction>0.0748205937641256</VolumetricFraction>
+ <PartialVolume>0.146373110632977</PartialVolume>
+ <VolumetricFlow>0.000107436429776567</VolumetricFlow>
+ <VolumetricFraction>0.942121964187232</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -5020,29 +4651,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.000885402917109643</compressibilityFactor>
- <density>994.725339949722</density>
- <enthalpy>-51.6540322281299</enthalpy>
- <entropy>-0.18093523431587</entropy>
+ <compressibilityFactor>0.00189559630481306</compressibilityFactor>
+ <density>764.023496425106</density>
+ <enthalpy>0.135692785336217</enthalpy>
+ <entropy>0.000455113855428359</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>1.23050660690151E-06</kinematic_viscosity>
- <massflow>0.00557173091921399</massflow>
+ <kinematic_viscosity>6.93814524133691E-07</kinematic_viscosity>
+ <massflow>0.0871266776930916</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>-973.014608554806</molar_enthalpy>
- <molar_entropy>-3.40830364247446</molar_entropy>
- <molarflow>0.29578422146715</molarflow>
+ <molar_enthalpy>9.89255406379874</molar_enthalpy>
+ <molar_entropy>0.0331796448046473</molar_entropy>
+ <molarflow>1.19508688019508</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>18.8371471999996</molecularWeight>
- <thermalConductivity>0.538574739113174</thermalConductivity>
- <viscosity>0.00122401610286048</viscosity>
- <volumetric_flow>5.6012757446147E-06</volumetric_flow>
+ <molecularWeight>72.9040533679604</molecularWeight>
+ <thermalConductivity>0.129670963284751</thermalConductivity>
+ <viscosity>0.000530090598599144</viscosity>
+ <volumetric_flow>0.000114036646910416</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.111562161263905</helmholtz_energy>
- <internal_energy>-51.7655943893938</internal_energy>
+ <helmholtz_energy>-0.064452667818253</helmholtz_energy>
+ <internal_energy>0.0712401175179639</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-2.10151285367827</molar_helmholtz_energy>
- <molar_internal_energy>-975.116121408485</molar_internal_energy>
+ <molar_helmholtz_energy>-4.69886073432934</molar_helmholtz_energy>
+ <molar_internal_energy>5.19369332946941</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -5054,8 +4685,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>6.03599946450972E-12</MassFraction>
- <MoleFraction>2.12621094659365E-12</MoleFraction>
+ <MassFraction>1.85304049459646E-15</MassFraction>
+ <MoleFraction>2.77548445309917E-15</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -5064,11 +4695,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>2.15438324163602E-07</PartialPressure>
- <PartialVolume>66.4993396309931</PartialVolume>
+ <PartialPressure>2.81225962210273E-10</PartialPressure>
+ <PartialVolume>16.3333857403832</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>3.74935194971271E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>4.04532613892299E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5079,8 +4710,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.854390513077169</MassFraction>
- <MoleFraction>0.97027029391199</MoleFraction>
+ <MassFraction>0.0332891487448025</MassFraction>
+ <MoleFraction>0.160744358234303</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -5089,11 +4720,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>98312.6375306324</PartialPressure>
- <PartialVolume>20.6270999065661</PartialVolume>
+ <PartialPressure>16287.4220980907</PartialPressure>
+ <PartialVolume>5.06637180683135</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.01067300000863E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>2.16939571234033E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5104,8 +4735,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.145609486916795</MassFraction>
- <MoleFraction>0.0297297060858838</MoleFraction>
+ <MassFraction>0.966710851255196</MassFraction>
+ <MoleFraction>0.839255641765695</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -5114,11 +4745,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>3012.36246915218</PartialPressure>
- <PartialVolume>114.729089130878</PartialVolume>
+ <PartialPressure>85037.577901909</PartialPressure>
+ <PartialVolume>28.1794447706677</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>1.6921657087555E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>1.82574542609751E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5147,23 +4778,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>19.1638012334567</ActivityCoeff>
+ <ActivityCoeff>8.55080688225902</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.89784817887196E-14</MassFraction>
- <MoleFraction>9.3987605031104E-15</MoleFraction>
- <Molarity>4.96316408068559E-10</Molarity>
+ <MassFraction>5.53019096224656E-17</MassFraction>
+ <MoleFraction>6.94179247569153E-17</MoleFraction>
+ <Molarity>7.27489393760675E-13</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>3.26945020389596</FugacityCoeff>
+ <FugacityCoeff>2.58797311511585</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>1.61460302974089E-16</MassFlow>
- <MolarFlow>2.78000505816871E-15</MolarFlow>
+ <MassFlow>4.81827165548904E-18</MassFlow>
+ <MolarFlow>8.2960451127359E-17</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>9.52329407977661E-10</PartialPressure>
- <PartialVolume>0.0724941596865831</PartialVolume>
- <VolumetricFlow>1.97803980318681E-19</VolumetricFlow>
- <VolumetricFraction>3.53140943844548E-14</VolumetricFraction>
- <DiffusionCoefficient>1.42353760645352E-09</DiffusionCoefficient>
+ <PartialPressure>7.03377122599444E-12</PartialPressure>
+ <PartialVolume>0.0737985565649378</PartialVolume>
+ <VolumetricFlow>5.63025263354846E-21</VolumetricFlow>
+ <VolumetricFraction>4.9372309569672E-17</VolumetricFraction>
+ <DiffusionCoefficient>3.39636755586633E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5172,23 +4803,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00075912902388</ActivityCoeff>
+ <ActivityCoeff>1.00071618575959</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.94680617031014</MassFraction>
- <MoleFraction>0.99</MoleFraction>
- <Molarity>52278.5152175403</Molarity>
+ <MassFraction>0.082076281663556</MassFraction>
+ <MoleFraction>0.332145468660139</MoleFraction>
+ <Molarity>3480.83447441072</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0141648993755611</FugacityCoeff>
+ <FugacityCoeff>0.0313458311213134</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00527534921361959</MassFlow>
- <MolarFlow>0.292826379252479</MolarFlow>
+ <MassFlow>0.00715103373874805</MassFlow>
+ <MolarFlow>0.39694269191198</MolarFlow>
<Name>Water</Name>
- <PartialPressure>100311.75</PartialPressure>
- <PartialVolume>0.0180308538169985</PartialVolume>
- <VolumetricFlow>5.18218496756583E-06</VolumetricFlow>
- <VolumetricFraction>0.925179406235839</VolumetricFraction>
- <DiffusionCoefficient>1.82705407394599E-09</DiffusionCoefficient>
+ <PartialPressure>33654.6396119886</PartialPressure>
+ <PartialVolume>0.0180809607203663</PartialVolume>
+ <VolumetricFlow>6.60021713384904E-06</VolumetricFlow>
+ <VolumetricFraction>0.0578780358127679</VolumetricFraction>
+ <DiffusionCoefficient>4.39866535046239E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5197,23 +4828,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.0059169097718</ActivityCoeff>
+ <ActivityCoeff>1.00551399949345</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0531938296898311</MassFraction>
- <MoleFraction>0.0099999999999906</MoleFraction>
- <Molarity>528.065810277688</Molarity>
+ <MassFraction>0.917923718336444</MassFraction>
+ <MoleFraction>0.667854531339861</MoleFraction>
+ <Molarity>6999.0148772973</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0429681414381261</FugacityCoeff>
+ <FugacityCoeff>0.0813925724333473</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.000296381705594235</MassFlow>
- <MolarFlow>0.00295784221466872</MolarFlow>
+ <MassFlow>0.0799756439543436</MassFlow>
+ <MolarFlow>0.798144188283104</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>1013.24999999905</PartialPressure>
- <PartialVolume>0.144359935789163</PartialVolume>
- <VolumetricFlow>4.19090777048666E-07</VolumetricFlow>
- <VolumetricFraction>0.0748205937641256</VolumetricFraction>
- <DiffusionCoefficient>1.23683240462953E-09</DiffusionCoefficient>
+ <PartialPressure>67670.3603880114</PartialPressure>
+ <PartialVolume>0.146373110632977</PartialVolume>
+ <VolumetricFlow>0.000107436429776567</VolumetricFlow>
+ <VolumetricFraction>0.942121964187232</VolumetricFraction>
+ <DiffusionCoefficient>2.95797656705226E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5227,36 +4858,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.000885402917109643</compressibilityFactor>
- <density>994.725339949722</density>
- <enthalpy>-51.6540322281299</enthalpy>
- <enthalpyF>-12861.9356230629</enthalpyF>
- <entropy>-0.18093523431587</entropy>
- <entropyF>-0.180935234316329</entropyF>
+ <compressibilityFactor>0.00189559630481306</compressibilityFactor>
+ <density>764.023496425106</density>
+ <enthalpy>0.135692785336217</enthalpy>
+ <enthalpyF>-2854.27393502409</enthalpyF>
+ <entropy>0.000455113855428359</entropy>
+ <entropyF>0.000455113855427484</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>1.23050660690151E-06</kinematic_viscosity>
- <massflow>0.00557173091921399</massflow>
+ <kinematic_viscosity>6.93814524133691E-07</kinematic_viscosity>
+ <massflow>0.0871266776930916</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>-973.014608554806</molar_enthalpy>
- <molar_entropy>-3.40830364247446</molar_entropy>
- <molarflow>0.29578422146715</molarflow>
+ <molar_enthalpy>9.89255406379874</molar_enthalpy>
+ <molar_entropy>0.0331796448046473</molar_entropy>
+ <molarflow>1.19508688019508</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>18.8371471999996</molecularWeight>
+ <molecularWeight>72.9040533679604</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.538574739113174</thermalConductivity>
- <viscosity>0.00122401610286048</viscosity>
- <volumetric_flow>5.6012757446147E-06</volumetric_flow>
- <bulk_modulus>1149.00632811195</bulk_modulus>
+ <thermalConductivity>0.129670963284751</thermalConductivity>
+ <viscosity>0.000530090598599144</viscosity>
+ <volumetric_flow>0.000114036646910416</volumetric_flow>
+ <bulk_modulus>-94.4570996686515</bulk_modulus>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.111562161263905</helmholtz_energy>
- <internal_energy>-51.7655943893938</internal_energy>
- <isothermal_compressibility>0.000870317225879169</isothermal_compressibility>
+ <helmholtz_energy>-0.064452667818253</helmholtz_energy>
+ <internal_energy>0.0712401175179639</internal_energy>
+ <isothermal_compressibility>-0.0105868166978229</isothermal_compressibility>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-2.10151285367827</molar_helmholtz_energy>
- <molar_internal_energy>-975.116121408485</molar_internal_energy>
- <idealGasHeatCapacityCp>1.84749766545925</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.31388289459456</idealGasHeatCapacityRatio>
+ <molar_helmholtz_energy>-4.69886073432934</molar_helmholtz_energy>
+ <molar_internal_energy>5.19369332946941</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.65181093265527</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.07415949807471</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -5279,7 +4910,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0724941596865831</PartialVolume>
+ <PartialVolume>0.0737985565649378</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5304,7 +4935,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0180308538169985</PartialVolume>
+ <PartialVolume>0.0180809607203663</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5329,7 +4960,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.144359935789163</PartialVolume>
+ <PartialVolume>0.146373110632977</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5363,8 +4994,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -5374,7 +5003,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0724941596865831</PartialVolume>
+ <PartialVolume>0.0737985565649378</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5388,8 +5017,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -5399,7 +5026,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180308538169985</PartialVolume>
+ <PartialVolume>0.0180809607203663</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5413,8 +5040,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -5424,7 +5049,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.144359935789163</PartialVolume>
+ <PartialVolume>0.146373110632977</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5458,8 +5083,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -5469,7 +5092,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0724941596865831</PartialVolume>
+ <PartialVolume>0.0737985565649378</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5483,8 +5106,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -5494,7 +5115,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180308538169985</PartialVolume>
+ <PartialVolume>0.0180809607203663</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5508,8 +5129,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -5519,7 +5138,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.144359935789163</PartialVolume>
+ <PartialVolume>0.146373110632977</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5564,7 +5183,7 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0724941596865831</PartialVolume>
+ <PartialVolume>0.0737985565649378</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5589,7 +5208,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180308538169985</PartialVolume>
+ <PartialVolume>0.0180809607203663</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5614,7 +5233,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.144359935789163</PartialVolume>
+ <PartialVolume>0.146373110632977</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -5642,16 +5261,27 @@ </Phases>
</SimulationObject>
<SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.Mixer</Type>
- <ObjectClass>MixersSplitters</ObjectClass>
+ <Type>DWSIM.UnitOperations.UnitOperations.CapeOpenUO</Type>
+ <ObjectClass>CAPEOPEN</ObjectClass>
+ <EmbeddedImageData></EmbeddedImageData>
+ <UseEmbeddedImage>false</UseEmbeddedImage>
<SupportsDynamicMode>true</SupportsDynamicMode>
<HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <PressureCalculation>Minimum</PressureCalculation>
- <MobileCompatible>true</MobileCompatible>
+ <ReactionSetID>DefaultSet</ReactionSetID>
+ <ReactionSetName></ReactionSetName>
+ <RecalcOutputStreams>true</RecalcOutputStreams>
+ <MobileCompatible>false</MobileCompatible>
+ <ProductName>ChemSep Column / Flash</ProductName>
+ <ProductDescription>ChemSep CAPE-OPEN Unit Operation</ProductDescription>
+ <ProductAuthor>Copyright (C) Ross Taylor and Harry Kooijman 2020</ProductAuthor>
+ <ProductContactInfo></ProductContactInfo>
+ <ProductPage>http://www.chemsep.com/</ProductPage>
+ <ProductVersion>2.0.0.10</ProductVersion>
+ <ProductAssembly>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</ProductAssembly>
<ExternalSolverID></ExternalSolverID>
<ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>Misturador</ComponentDescription>
- <ComponentName>MIST-ae80e666-b984-4270-b427-05f406124fe0</ComponentName>
+ <ComponentDescription>CapeOpenUnitOperation</ComponentDescription>
+ <ComponentName>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</ComponentName>
<IsDirty>true</IsDirty>
<CanUsePreviousResults>false</CanUsePreviousResults>
<DynamicsSpec>Pressure</DynamicsSpec>
@@ -5663,7 +5293,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:22</LastUpdated>
+ <LastUpdated>04/13/2024 20:23:59</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -5671,15 +5302,75 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MIST-ae80e666-b984-4270-b427-05f406124fe0</Name>
+ <Name>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</Name>
+ <UserDefinedChartNames />
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+ <CAPEOPEN_Object_Info>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.CapeOpen.CapeOpenUnitOpInfo</Type>
+ <TypeName>ChemSepUO.ChemSep_UnitOperation.1</TypeName>
+ <Version>2.0.0.10</Version>
+ <Description>ChemSep CAPE-OPEN Unit Operation</Description>
+ <HelpURL></HelpURL>
+ <VendorURL>http://www.chemsep.com/</VendorURL>
+ <AboutInfo>Copyright (C) Ross Taylor and Harry Kooijman 2020</AboutInfo>
+ <CapeVersion>1.0</CapeVersion>
+ <Location>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</Location>
+ <Name>ChemSep Column / Flash</Name>
+ <ImplementedCategory></ImplementedCategory>
+ </CAPEOPEN_Object_Info>
+ 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GluZTIgeD0wLjYyNSB5PTAuODI1IC8+DQo8bGluZTIgeD0wLjYwNSB5PTAuODM1IC8+DQo8bGluZTIgeD0wLjYwNSB5PTAuODE1IC8+DQo8bGluZTIgeD0wLjYyNSB5PTAuODI1IC8+DQo8ZWxsaXBzZSB4MT0wLjYyNSB5MT0wLjkgeDI9MC43NzUgeTI9MC43NSAvPg0KPG1vdmUyIHg9MC43NzUgeT0wLjkgLz4NCjxsaW5lMiB4PTAuNjI1IHk9MC43NSAvPg0KPGxpbmUyIHg9MC42NDYyMTMgeT0wLjc1NzA3MSAvPg0KPG1vdmUyIHg9MC42MjUgeT0wLjc1IC8+DQo8bGluZTIgeD0wLjYzMjA3MSB5PTAuNzcxMjEzIC8+DQo8bW92ZTIgeD0wLjcgeT0wLjc1IC8+DQo8bGluZTIgeD0wLjcgeT0wLjcgLz4NCjxzdHJpbmcgeD0wLjcxIHk9MC43NSBzPSIxIiAvPg0KPG1vdmUyIHg9MC43IHk9MC43IC8+DQo8bGluZTIgeD0wLjU1IHk9MC43IC8+DQo8bGluZTIgeD0wLjU3IHk9MC42OSAvPg0KPGxpbmUyIHg9MC41NyB5PTAuNzEgLz4NCjxsaW5lMiB4PTAuNTUgeT0wLjcgLz4NCjxtb3ZlMiB4PTAuNTUgeT0wLjcgLz4NCjxsaW5lMiB4PTAuOSB5PTAuNyAvPg0KPGxpbmUyIHg9MC44OCB5PTAuNzEgLz4NCjxsaW5lMiB4PTAuODggeT0wLjY5IC8+DQo8bGluZTIgeD0wLjkgeT0wLjcgLz4NCjxzdHJpbmcgeD0wLjgwMTI5OCB5PTAuNzUzNDM1IHM9IlRvcCIgLz4NCjxtb3ZlMiB4PTAuNDUgeT0wLjI1IC8+DQo8bGluZTIgeD0wLjQ1IHk9MC4xNzUgLz4NCjxtb3ZlMiB4PTAuNDUgeT0wLjE3NSAvPg0KPGxpbmUyIHg9MC42MjUgeT0wLjE3NSAvPg0KPGxpbmUyIHg9MC42MDUgeT0wLjE4NSAvPg0KPGxpbmUyIHg9MC42MDUgeT0wLjE2NSAvPg0KPGxpbmUyIHg9MC42MjUgeT0wLjE3NSAvPg0KPGVsbGlwc2UgeDE9MC42MjUgeTE9MC4yNSB4Mj0wLjc3NSB5Mj0wLjEgLz4NCjxtb3ZlMiB4PTAuNjI1IHk9MC4xIC8+DQo8bGluZTIgeD0wLjc3NSB5PTAuMjUgLz4NCjxsaW5lMiB4PTAuNzUzNzg3IHk9MC4yNDI5MjkgLz4NCjxtb3ZlMiB4PTAuNzc1IHk9MC4yNSAvPg0KPGxpbmUyIHg9MC43Njc5MjkgeT0wLjIyODc4NyAvPg0KPG1vdmUyIHg9MC43IHk9MC4yNSAvPg0KPGxpbmUyIHg9MC43IHk9MC4zIC8+DQo8c3RyaW5nIHg9MC42NzcwOTkgeT0wLjE2MzQzNSBzPSIzMiIgLz4NCjxtb3ZlMiB4PTAuNyB5PTAuMyAvPg0KPGxpbmUyIHg9MC41NSB5PTAuMyAvPg0KPGxpbmUyIHg9MC41NyB5PTAuMjkgLz4NCjxsaW5lMiB4PTAuNTcgeT0wLjMxIC8+DQo8bGluZTIgeD0wLjU1IHk9MC4zIC8+DQo8bW92ZTIgeD0wLjc3NSB5PTAuMTc1IC8+DQo8bGluZTIgeD0wLjkgeT0wLjE3NSAvPg0KPGxpbmUyIHg9MC44OCB5PTAuMTg1IC8+DQo8bGluZTIgeD0wLjg4IHk9MC4xNjUgLz4NCjxsaW5lMiB4PTAuOSB5PTAuMTc1IC8+DQo8c3RyaW5nIHg9MC43NDQwNDYgeT0wLjIyODQzNSBzPSJCb3R0b20iIC8+DQo8bW92ZTIgeD0wLjM1IHk9MC42NzI0MTQgLz4NCjxsaW5lMiB4PTAuNTUgeT0wLjY3MjQxNCAvPg0KPG1vdmUyIHg9MC4xIHk9MC42NzI0MTQgLz4NCjxsaW5lMiB4PTAuMzUgeT0wLjY3MjQxNCAvPg0KPGxpbmUyIHg9MC4zMyB5PTAuNjgyNDE0IC8+DQo8bGluZTIgeD0wLjMzIHk9MC42NjI0MTQgLz4NCjxsaW5lMiB4PTAuMzUgeT0wLjY3MjQxNCAvPg0KPHN0cmluZyB4PTAuMzcgeT0wLjcyNTg0OSBzPSI0IiAvPg0KPHN0cmluZyB4PTAuMSB5PTAuNzI1ODQ5IHM9IkZlZWQyIiAvPg0KPG1vdmUyIHg9MC4zNSB5PTAuNTA2ODk3IC8+DQo8bGluZTIgeD0wLjU1IHk9MC41MDY4OTcgLz4NCjxtb3ZlMiB4PTAuMSB5PTAuNTA2ODk3IC8+DQo8bGluZTIgeD0wLjM1IHk9MC41MDY4OTcgLz4NCjxsaW5lMiB4PTAuMzMgeT0wLjUxNjg5NyAvPg0KPGxpbmUyIHg9MC4zMyB5PTAuNDk2ODk3IC8+DQo8bGluZTIgeD0wLjM1IHk9MC41MDY4OTcgLz4NCjxzdHJpbmcgeD0wLjM3IHk9MC41NjAzMzIgcz0iMTYiIC8+DQo8c3RyaW5nIHg9MC4xIHk9MC41NjAzMzIgcz0iRmVlZDEiIC8+DQo8L3N2Zz4NCg0KW0NvQ29dDQo8aWNvbiBjaGs9IjMyNjY4Ij4NCiMgQ29jbyBjb2x1bW4gaWNvbiBnZW5lcmF0ZWQgYnkgQ2hlbVNlcA0KIyBTaXplcw0KV0lEVEggMTQNCkhFSUdIVCAzOA0KREVGSEVJR0hUIDM4DQpYR1JPVyA0DQpZR1JPVyAxOQ0KIyBjb2x1bW4gKyBJbnRlcm5hbHMNCkJPRFkgMCA0IDggMzQgLTEgNA0KIyBzdGFnZQ0KTElORSBEQVNIRUQgMCA4IDggOA0KVEVYVCA0IDcgMg0KTElORSBEQVNIRUQgMCAzMCA4IDMwDQpURVhUIDQgMzEgMzENCiMgVG90YWwgQ29uZGVuc2VyDQojIGNvbmRlbnNlcg0KQk9EWSAxMCAwIDE0IDQgIC0xIC0xDQojIG92ZXJoZWFkIGxpbmUgdXANCkxJTkUgNCA0IDQgMg0KIyBvdmVyaGVhZCB0byBDDQpMSU5FIEFSUk9XIDQgMiAxMCAyDQojIHJlZmx1eCBsaW5lIGRvd24NCkxJTkUgMTIgNCAxMiA4DQojIHJlZmx1eA0KTElORSBBUlJPVyAxMiA4IDggOA0KIyBoZWF0IGV4Y2hhbmdlZA0KTElORSBUSElOTElORSBPQVJST1cgMTQgMCAxMCA0DQojIGhlYXQgc3RyZWFtDQpDT05ORUNUSU9OIDE0IDANCiMgZGlzdGlsbGF0ZSBsaW5lDQpMSU5FIDEyIDggMTQgOA0KIyBkaXN0aWxsYXRlIGNvbm5lY3Rvcg0KQ09OTkVDVElPTiAxNCA4DQojIFBhcnRpYWwgUmVib2lsZXINCiMgUmVib2lsZXINCkJPRFkgMTAgMzQgMTQgMzggIC0xIC0xDQojIGJvdHRvbXMgbGluZSBkb3duDQpMSU5FIDQgMzQgNCAzNg0KIyBib3R0b21zIHRvIFINCkxJTkUgQVJST1cgNCAzNiAxMCAzNg0KIyBoZWF0IGV4Y2hhbmdlZA0KTElORSBUSElOTElORSBPQVJST1cgMTAgMzggMTQgMzQNCiMgaGVhdCBzdHJlYW0NCkNPTk5FQ1RJT04gMTAgMzgNCiMgcmVib2lsIGxpbmUgdXANCkxJTkUgMTIgMzQgMTIgMzANCiMgcmVib2lsDQpMSU5FIEFSUk9XIDEyIDMwIDggMzANCiMgYm90dG9tcyBwcm9kdWN0IGNvbm5lY3Rvcg0KQ09OTkVDVElPTiAxMiAzOA0KIyBib3R0b21zIHByb2R1Y3QgY29ubmVjdG9yDQpDT05ORUNUSU9OIDE0IDM2DQojIENvbm5lY3Rpb25zIGFuZCBmcmVlIHNwYWNlIGZvciBmZWVkcyBhbmQgc2lkZXN0cmVhbXMNClZDT05ORUNUSU9OIDAgOCAzMA0KVkNPTk5FQ1RJT04gOCA5IDI5DQpGUkVFU1BBQ0UgOSA5IDEyIDI5DQpGUkVFU1BBQ0UgMTMgOSAxNCAyOQ0KTElORSBEQVNIRUQgMCAxMCA4IDEwDQojIHN0YWdlDQpURVhUIDQgOSA0DQpMSU5FIERBU0hFRCAwIDE5IDggMTkNCiMgc3RhZ2UNClRFWFQgNCAxOCAxNg0KPC9pY29uPg0KDQpbU2V0dGluZ3NdDQo8R3JhcGhzPg0KMCBsYXN0ICMgc3RhZ2VzDQpDb21ib0JveD1Db21ib0JveDE0DQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3gyMA0KLTENCkNvbWJvQm94PUNvbWJvQm94MjENCi0xDQpDaGVja0JveD1DaGVja0JveDMNCjAgU2hvdyBzZXR0aW5ncw0KQ2hlY2tCb3g9Q2hlY2tCb3gxDQoxIEF1dG8gY29sb3JzDQpDaGVja0JveD1DaGVja0JveDINCjEgQXV0byBwb2ludHMNCkVkaXQ9RWRpdDkNCjAuMg0KU3RyaW5nR3JpZD1TdHJpbmdHcmlkNQ0KMg0KOA0KVGl0bGUNCkxhYmVscw0KU3RhZ2VzDQpBeGlzIGNvbG9yDQpDb21tYW5kcw0KQm94DQpMYWJlbHMgYm94DQpJbXBvcnQgZGF0YQ0KDQoNCg0KDQoNCg0KDQoNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDQNCjUNCjkNCg0KVGl0bGUNClN0YXJ0DQpFbmQNClRpYyBpbnRlcnZhbA0KU21hbGwgdGljcw0KR3JpZA0KTG9nYXJpdGhtaWMNClNjaWVudGlmaWMgbm90YXRpb24NCngxDQoNCg0KDQoNCg0KDQoNCg0KeTENCg0KDQoNCg0KDQoNCg0KDQp4Mg0KDQoNCg0KDQoNCg0KDQoNCnkyDQoNCg0KDQoNCg0KDQoNCg0KU3RyaW5nR3JpZD1TdHJpbmdHcmlkMw0KMg0KMTQNCg0KTGFiZWwNClBsb3QgWA0KUGxvdCBZDQpYIGF4aXMNClkgYXhpcw0KVW5pdHMgWA0KVW5pdHMgWQ0KQ29sb3INClBvaW50cw0KVGhpY2tuZXNzDQpTdHlsZQ0KMXN0IHN0YWdlDQpMYXN0IHN0YWdlDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KPC9HcmFwaHM+DQo8TWNDYWJlLVRoaWVsZT4NClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uNg0KMSBBdXRvLXNlbGVjdCBrZXkgY29tcG9uZW50cw0KQ29tYm9Cb3g9Q29tYm9Cb3gyMg0KLTENCkNvbWJvQm94PUNvbWJvQm94MjMNCi0xDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQ3DQoxNg0KMg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDExDQo1DQozDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQpDaGVja0JveD1DaGVja0JveDQ1DQowIEx1bXBlZA0KPC9NY0NhYmUtVGhpZWxlPg0KPEZVRz4NCkNvbWJvQm94PUNvbWJvQm94NzUNCi0xDQpDb21ib0JveD1Db21ib0JveDc2DQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3g3Nw0KLTENCkVkaXQ9RWRpdDU1DQowLjk1DQpFZGl0PUVkaXQ1Ng0KMC45NQ0KRWRpdD1FZGl0NTcNCjEuMg0KPC9GVUc+DQo8UGFyYW1ldHJpeD4NCkVkaXQ9RWRpdDENCjENCkNoZWNrQm94PUNoZWNrQm94Mg0KMCBVc2Ugb2xkIHJlc3VsdHMNCkNoZWNrQm94PUNoZWNrQm94Mw0KMSBBdXRvbWF0aWMNCkNoZWNrQm94PUNoZWNrQm94MQ0KMCBLZWVwIHNlcC1maWxlcw0KQ2hlY2tCb3g9Q2hlY2tCb3g0DQoxIFJlc3RvcmUgb3JpZ2luYWwNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDENCjENCjYNCk5hbWUNClZhcmlhYmxlDQpVbml0cw0KVmFsdWUNClN0YXJ0L1ZhbHVlbGlzdA0KRW5kDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQyDQo0DQoxDQpOYW1lDQpWYXJpYWJsZQ0KVW5pdHMNCkN1cnJlbnQgVmFsdWUNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDMNCjENCjENCk5vbmUNCjwvUGFyYW1ldHJpeD4NCjxCaW5hcnlQaGFzZURpYWdyYW0+DQpDb21ib0JveD1Db21ib0JveDENCi0xDQpDb21ib0JveD1Db21ib0JveDINCi0xDQpDb21ib0JveD1Db21ib0JveDIxDQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3gyMw0KLTENCkNvbWJvQm94PUNvbWJvQm94Mw0KLTENCkNvbWJvQm94PUNvbWJvQm94NQ0KLTENCkVkaXQ9RWRpdDENCg0KRWRpdD1FZGl0Mg0KNTENCkVkaXQ9RWRpdDExDQoxZS01DQpFZGl0PUVkaXQxMg0KMQ0KRWRpdD1FZGl0Mw0KDQpDb21ib0JveD1Db21ib0JveDQNCjANCkZvbnQ9QlZMRWZvbnQNCjk2DQotMTY3NzcyMDgNCk1TIFNhbnMgU2VyaWYNCi04DQowDQpDaGVja0JveD1DaGVja0JveDINCjEgDQpDb2xvcj1FZGl0MTgNCi0xNjc3NzIwOA0KQ2hlY2tCb3g9Q2hlY2tCb3g2DQoxIExlZ2VuZA0KQ29tYm9Cb3g9Q29tYm9Cb3gxNQ0KMA0KU3BpbkVkaXQ9U3BpbkVkaXQxDQoxDQpDaGVja0JveD1DaGVja0JveDMNCjAgDQpDb2xvcj1FZGl0MTkNCi0xNjc3NzIxMQ0KRWRpdD1FZGl0NQ0KDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQyDQo3DQoyDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KU3RyaW5nR3JpZD1TdHJpbmdHcmlkMw0KNw0KMg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDQNCjcNCjINCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQpDb2xvcj1CVkxFYnBsaW5lQ29sb3INCjE2Nzc3MjE1DQpTcGluRWRpdD1TcGluRWRpdDINCjENCkNvbWJvQm94PUNvbWJvQm94MTMNCjANClNwaW5FZGl0PVNwaW5FZGl0NA0KMg0KQ29sb3I9QlZMRWRwbGluZUNvbG9yDQoxNjc3NzIxNQ0KU3BpbkVkaXQ9U3BpbkVkaXQzDQoxDQpDb21ib0JveD1Db21ib0JveDE0DQowDQpTcGluRWRpdD1TcGluRWRpdDUNCjINClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uMw0KMSBGaXhlZCBjb2xvcnMNClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uMg0KMCBDb2xvciBwZXIgc2V0Og0KRHJhd1NldENvbG9ycz1CVkxFY29sb3JzDQoxMzE4MTQNCjE0Mjk2NjI4DQoyMTkzMTANCjExMjcyMzY0DQoyNDU4ODgxDQoxMDA1MjM1Mg0KMzYxODYxNQ0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KMA0KQ29tYm9Cb3g9Q29tYm9Cb3g3DQoxDQpDb21ib0JveD1Db21ib0JveDExDQoxDQpDb21ib0JveD1Db21ib0JveDYNCjMNClNwaW5FZGl0PVNwaW5FZGl0Ng0KMg0KTWVtbz1NZW1vMQ0KMTUNCiMgZGF0YSBzZXRzIGFyZSBlbnRlcmVkIGJ5IHNldHRpbmcgYSBrZXl3b3JkLCBlLGcsICJweHkiLCAiVHh5IiwgInhUIiwgb3IgIlR4cSINCiMgZGF0YSBpcyB0aGVuIGVudGVyZWQgc2VwYXJhdGVkIGJ5IHNwYWNlcyBvciB0YWJzIGFuZCBlYWNoIGxpbmUgdGVybWluYXRlIHdpdGggYSAiOyINCiMgfiBzaWduYWxzIHRoZSBzdGFydCBvZiBhIG5ldyBkYXRhIHNldC4gT3B0aW9uYWwgYXJlIG5hbWUgYW5kIGNvbXBvbmVudCBpbmRleCBvZiB0aGUgdmFyaWFibGUNCiMgdGh1cyB+IHAgMCB4IDMgeiA1IGEgNyBAVD0zMjMuMTUgc2V0cyB0aGUgdHlwZSB0byBweHphIHdoZXJlIHggaXMgY29tcG9uZW50IDMsIA0KIyB6IGNvbXBvbmVudCA1LCBhIGNvbXBvbmVudCA3LCBhbmQgdGhlIHRlbXBlcmF0dXJlIHRvIDMyMy4xNUsNCiMgYSBsZWdlbmQgZW50cnkgY2FuIGJlIGFkZGVkIGJ5IGluY2x1ZGluZyBhIGxpbmUgIkxHRD1EZXNjcmlwdGlvbiINCiMgVCA9IHRlbXBlcmF0dXJlIGluIEssIHAgPSBwcmVzc3VyZSBpbiBQYSwgeCBhbmQgeSBhcmUgbGlxdWlkIGFuZCB2YXBvciBjb21wb3NpdGlvbnMNCiMgcSBhbmQgeiBhcmUgY2FsY3VsYXRlZCBidWJibGUgYW5kIGRldyBlcXVpbGlicml1bSBwb2ludHMgKHdoZW4gZGV2aWF0aW9uIGlzIHNlbGVjdGVkKQ0KIyB0aGUgbGF0dGVyIGFyZSBjb21wdXRlZCB2aWEgaW50ZXJwb2xhdGlvbiBvZiB0aGUgY29tcHV0ZWQgbGluZXMgdGhhdCBiZWxvbmcgdG8gdGhlIGRhdGEgc2V0DQojIHRleHQgbGFiZWxzIGNhbiBiZSBhZGRlZCBieSAieCB5IHRleHQiDQojIGxpbmVzIHN0YXJ0aW5nIHdpdGggYSAjIGlzIHJlZ2FyZGVkIGFzIGEgY29tbWVudA0KIyB0aGUgbGVnZW5kIGNhbiBiZSBwbGFjZWQgYnkgc3BlY3lpbmcgY29ybmVyIExlZnQgVG9wIHdpdGggIkxHRExUIg0KIyBhIHRleHQgYm94IGNhbiBiZSBhZGRlZCBieSAiRC1UZXh0Qm94IHggeSBUaGlzIGlzIGEgYm94IiwNCiMgd2hlcmUgWCBhbmQgWSBhcmUgY29vcmRpbmF0ZXMgaW4gdGhlIHJhbmdlIGZyb20gMCB0byAxDQojIEQtTGluZSB4MSB5MSB4MiB5MiBkcmF3cyBhIGxpbmUgYW5kIG90aGVyIHByaW1pdGl2ZXMgYXJlIGF2YWlsYWJsZQ0KQ29tYm9Cb3g9Q29tYm9Cb3gxNw0KMA0KQ29tYm9Cb3g9Q29tYm9Cb3gxOA0KMg0KQ29tYm9Cb3g9Q29tYm9Cb3gxOQ0KMA0KQ29tYm9Cb3g9Q29tYm9Cb3gyMg0KLTENCkVkaXQ9RWRpdDQNCjENCkVkaXQ9RWRpdDYNCjENCkVkaXQ9RWRpdDcNCjENCkVkaXQ9RWRpdDgNCjENCkVkaXQ9RWRpdDkNCjIwDQpFZGl0PUVkaXQxMA0KMWUtNA0KVmFsdWVMaXN0RWRpdG9yPVZhbHVlTGlzdEVkaXRvcjENCjYNClBhcmFtZXRlcg0KVmFsdWUNClBhcmFtZXRlcg0KVmFsdWUNClBhcmFtZXRlcg0KVmFsdWUNClBhcmFtZXRlcg0KVmFsdWUNClBhcmFtZXRlcg0KVmFsdWUNClBhcmFtZXRlcg0KVmFsdWUNCnNlbGVjdCBhIHBhcmFtZXRlcg0KDQpDb21ib0JveD1Db21ib0JveDIwDQotMQ0KPC9CaW5hcnlQaGFzZURpYWdyYW0+DQo8VGVybmFyeVBoYXNlRGlhZ3JhbT4NCkNvbWJvQm94PUNvbWJvQm94MQ0KLTENCkNvbWJvQm94PUNvbWJvQm94Mg0KLTENCkNvbWJvQm94PUNvbWJvQm94Mw0KLTENCkNvbWJvQm94PUNvbWJvQm94NA0KLTENCkNvbWJvQm94PUNvbWJvQm94Nw0KLTENCkVkaXQ9RWRpdDENCg0KRWRpdD1FZGl0Mg0KMjENCkVkaXQ9RWRpdDkNCjANCkVkaXQ9RWRpdDEwDQowLjINCkVkaXQ9RWRpdDMNCg0KQ29tYm9Cb3g9Q29tYm9Cb3gxMg0KMA0KRm9udD1UVkxFZm9udA0KOTYNCi0xNjc3NzIwOA0KTVMgU2FucyBTZXJpZg0KLTgNCjANClNwaW5FZGl0PVNwaW5FZGl0Mw0KMQ0KQ2hlY2tCb3g9Q2hlY2tCb3g0DQowIA0KQ29sb3I9RWRpdDEyDQotMTY3NzcyMTENCkVkaXQ9RWRpdDUNCg0KU3RyaW5nR3JpZD1TdHJpbmdHcmlkMg0KNw0KMg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDMNCjcNCjINCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQ0DQo3DQoyDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KQ29sb3I9VFZMRWJwbGluZUNvbG9yDQoxNjc3NzIxNQ0KU3BpbkVkaXQ9U3BpbkVkaXQxDQoxDQpDb21ib0JveD1Db21ib0JveDkNCjANClNwaW5FZGl0PVNwaW5FZGl0NA0KMg0KQ29sb3I9VFZMRWRwbGluZUNvbG9yDQoxNjc3NzIxNQ0KU3BpbkVkaXQ9U3BpbkVkaXQyDQoxDQpDb21ib0JveD1Db21ib0JveDEwDQowDQpTcGluRWRpdD1TcGluRWRpdDUNCjINClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uMQ0KMSBGaXhlZCBjb2xvcnMNClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uMg0KMCBDb2xvciBwZXIgc2V0DQpEcmF3U2V0Q29sb3JzPVRWTEVjb2xvcnMNCjEzMTgxNA0KMTQyOTY2MjgNCjIxOTMxMA0KMTEyNzIzNjQNCjI0NTg4ODENCjEwMDUyMzUyDQozNjE4NjE1DQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQo8L1Rlcm5hcnlQaGFzZURpYWdyYW0+DQo8QmluYXJ5UHJvcGVydHlEaWFncmFtPg0KQ29tYm9Cb3g9Q29tYm9Cb3gxDQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3gyDQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3gzDQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3g1DQotMQ0KQ29tYm9Cb3g9Q29tYm9Cb3g4DQotMQ0KRWRpdD1FZGl0MQ0KDQpFZGl0PUVkaXQyDQoNCkVkaXQ9RWRpdDYNCjANCkVkaXQ9RWRpdDcNCjENCkVkaXQ9RWRpdDMNCjUxDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQ3DQo1DQoyDQoNCg0KDQoNCg0KDQoNCg0KDQoNCkVkaXQ9RWRpdDQNCg0KQ29tYm9Cb3g9Q29tYm9Cb3gxMw0KMA0KRm9udD1CcHJvcGZvbnQNCjk2DQotMTY3NzcyMDgNCk1TIFNhbnMgU2VyaWYNCi04DQowDQpDaGVja0JveD1DaGVja0JveDINCjEgDQpDb2xvcj1FZGl0MTMNCi0xNjc3NzIwOA0KQ2hlY2tCb3g9Q2hlY2tCb3g1DQoxIExlZ2VuZA0KQ29tYm9Cb3g9Q29tYm9Cb3gxNA0KMA0KU3BpbkVkaXQ9U3BpbkVkaXQxDQoxDQpDaGVja0JveD1DaGVja0JveDMNCjAgDQpDb2xvcj1FZGl0MTQNCi0xNjc3NzIxMQ0KRWRpdD1FZGl0NQ0KDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQyDQo3DQoyDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KU3RyaW5nR3JpZD1TdHJpbmdHcmlkMw0KNw0KMg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNClN0cmluZ0dyaWQ9U3RyaW5nR3JpZDQNCjcNCjINCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQ1DQo3DQoyDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KU3RyaW5nR3JpZD1TdHJpbmdHcmlkNg0KNw0KMg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCkNvbG9yPUJwcm9wQWxpbmVDb2xvcg0KMTY3MTE2ODANClNwaW5FZGl0PVNwaW5FZGl0Mg0KMQ0KQ29tYm9Cb3g9Q29tYm9Cb3gxMA0KMA0KU3BpbkVkaXQ9U3BpbkVkaXQ1DQoyDQpDb2xvcj1CcHJvcEJsaW5lQ29sb3INCjI1NQ0KU3BpbkVkaXQ9U3BpbkVkaXQzDQoxDQpDb21ib0JveD1Db21ib0JveDExDQowDQpTcGluRWRpdD1TcGluRWRpdDYNCjINClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uMQ0KMSBGaXhlZCBjb2xvcnM6DQpSYWRpb0J1dHRvbj1SYWRpb0J1dHRvbjINCjAgQ29sb3IgcGVyIHNldDoNCkRyYXdTZXRDb2xvcnM9QnByb3BDb2xvcnMNCjEzMTgxNA0KMTQyOTY2MjgNCjIxOTMxMA0KMTEyNzIzNjQNCjI0NTg4ODENCjEwMDUyMzUyDQozNjE4NjE1DQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQowDQpDb21ib0JveD1Db21ib0JveDkNCjENCkNvbWJvQm94PUNvbWJvQm94Nw0KMQ0KQ29tYm9Cb3g9Q29tYm9Cb3g2DQozDQpTcGluRWRpdD1TcGluRWRpdDQNCjINCk1lbW89TWVtbzENCjEyDQojIGRhdGEgc2V0cyBhcmUgZW50ZXJlZCBieSBzZXR0aW5nIGEga2V5d29yZCwgZSxnLCAiQXgiLCAiQUJ4IiwgIkFUIiwgb3IgIkJwIg0KIyBkYXRhIGlzIHRoZW4gZW50ZXJlZCBzZXBhcmF0ZWQgYnkgc3BhY2VzIG9yIHRhYnMgYW5kIGVhY2ggbGluZSB0ZXJtaW5hdGUgd2l0aCBhICI7Ig0KIyBhICJ+IiBzaWduYWxzIGEgbmV3IGRhdGEgc2V0IA0KIyBUID0gdGVtcGVyYXR1cmUgaW4gSywgcCA9IHByZXNzdXJlIGluIFBhLCB4IGFuZCB5IGFyZSBsaXF1aWQgYW5kIHZhcG9yIGNvbXBvc2l0aW9ucw0KIyBBIGFuZCBCIGFyZSB0aGUgcHJvcGVydGllcyANCiMgdGV4dCBsYWJlbHMgY2FuIGJlIGFkZGVkIGJ5ICJ4IHkgdGV4dCINCiMgbGluZXMgc3RhcnRpbmcgd2l0aCBhICMgaXMgcmVnYXJkZWQgYXMgYSBjb21tZW50DQojIGEgbGVnZW5kIGNhbiBiZSBhZGRlZCBieSBpbmNsdWRpbmcgYSBsaW5lICJMR0QgRGVzY3JpcHRpb24iDQojIHRoZSBsZWdlbmQgY2FuIGJlIHBsYWNlZCBieSBzcGVjeWluZyBjb3JuZXIgTGVmdCBUb3Agd2l0aCAiTEdETFQiDQojIGEgdGV4dCBib3ggY2FuIGJlIGFkZGVkIGJ5ICJELVRleHRCb3ggeCB5IFRoaXMgaXMgYSBib3giLA0KIyB3aGVyZSBYIGFuZCBZIGFyZSBjb29yZGluYXRlcyBpbiB0aGUgcmFuZ2UgZnJvbSAwIHRvIDENCiMgRC1MaW5lIHgxIHkxIHgyIHkyIGRyYXdzIGEgbGluZSBhbmQgb3RoZXIgcHJpbWl0aXZlcyBhcmUgYXZhaWxhYmxlDQo8L0JpbmFyeVByb3BlcnR5RGlhZ3JhbT4NCjxSYXRpbmdQYW5lbD4NCkVkaXQ9RWRpdDYxDQoNCkVkaXQ9RWRpdDU4DQoxDQpFZGl0PUVkaXQ1OQ0KMC43NQ0KRWRpdD1FZGl0NjQNCjEuMA0KRWRpdD1FZGl0NjANCjAuOA0KRWRpdD1FZGl0ODUNCjEwDQpFZGl0PUVkaXQ4Ng0KMTgwDQpSYWRpb0J1dHRvbj1SYWRpb0J1dHRvbjExDQoxIEtvY2gNClJhZGlvQnV0dG9uPVJhZGlvQnV0dG9uMTINCjAgTm9ydG9uDQpSYWRpb0J1dHRvbj1SYWRpb0J1dHRvbjEzDQowIFNwZWNpZmllZA0KUmFkaW9CdXR0b249UmFkaW9CdXR0b245DQowIER1c3MtVGF5bG9yDQpSYWRpb0J1dHRvbj1SYWRpb0J1dHRvbjEwDQoxIFRyYWRpdGlvbmFsDQpTdHJpbmdHcmlkPVN0cmluZ0dyaWQyMg0KMTMNCjUNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQoNCg0KDQpDb21ib0JveD1Db21ib0JveDEwNA0KMg0KRWRpdD1FZGl0ODkNCjgNCkVkaXQ9RWRpdDkwDQozNQ0KRWRpdD1FZGl0NjcNCjAuMzINCkVkaXQ9RWRpdDYzDQo4MDE2DQpFZGl0P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QBtAGUAOgAgAEUARABDAC0AMAAxACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgAA0ACgBDAGEAcABlAC0ATwBwAGUAbgAgAHUAbgBpAHQAIABpAGQAOgAgAEMAUwBfADIAXwA0ADMAQQBDAF8AMQBEAEEAOABEAEIAMQBfADUANQAzADcAOAAyADgAMAAgACAAIAAgACAAIAANAAoAQwBhAHAAZQAtAE8AcABlAG4AIAByAHUAbgAgAGwAZQB2AGUAbAA6ACAAbgBvAHIAbQBhAGwAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAANAAoAQwBhAHAAZQAtAE8AcABlAG4AIABJAG4AaQB0AGkAYQBsAGkAegBlAGQADQAKAEMAYQBwAGUALQBPAHAAZQBuACAAVABoAGUAcgBtAG8AZAB5AG4AYQBtAGkAYwAtAHAAcgBvAHAAZQByAHQAaQBlAHMAIABkAGkAcwBhAGIAbABlAGQADQAKAFIAZQBhAGQAaQBuAGcAIABjAG8AbgBmAGkAZwB1AHIAYQB0AGkAbwBuAA0ACgBSAGUAYQBkAGkAbgBnACAAYwBvAG0AcABvAG4AZQBuAHQAIABwAHIAbwBwAGUAcgB0AHkAIABsAGkAYgByAGEAcgBpAGUAcwANAAoAUgBlAGEAZABpAG4AZwAgAHQAaABlAHIAbQBvAGQAeQBuAGEAbQBpAGMAIABwAHIAbwBwAGUAcgB0AHkAIABvAHAAdABpAG8AbgBzAA0ACgBLAC0AdgBhAGwAdQBlADoAIABEAEUAQwBIAEUATQBBAA0ACgBSAGUAYQBkAGkAbgBnACAAcABoAHkAcwBpAGMAYQBsACAAcAByAG8AcABlAHIAdAB5ACAAbwBwAHQAaQBvAG4AcwANAAoAUgBlAGEAZABpAG4AZwAgAHQAaABlAHIAbQBvAGQAeQBuAGEAbQBpAGMAIABwAHIAbwBwAGUAcgB0AHkAIABkAGEAdABhAA0ACgBXAGEAcgBuAGkAbgBnACEAIQAgAEUAcwB0AGkAbQBhAHQAaQBuAGcAIABhAGMAdABpAHYAaQB0AHkAIABtAG8AZABlAGwAIABwAGEAcgBhAG0AZQB0AGUAcgBzAA0ACgBSAGUAYQBkAGkAbgBnACAAcgBlAGEAYwB0AGkAbwBuACAAZABhAHQAYQANAAoAUgBlAGEAZABpAG4AZwAgAHMAcABlAGMAaQBmAGkAYwBhAHQAaQBvAG4AcwANAAoAQwBoAGUAYwBrAGkAbgBnACAAYwBvAG0AcABvAG4AZQBuAHQAcwAgAGQAYQB0AGEAIAAoADMAKQANAAoARABlAHQAZQByAG0AaQBuAGkAbgBnACAAZgBlAGUAZAAgAGMAbwBuAGQAaQB0AGkAbwBuAHMADQAKACAARgBlAGUAZAAtAGYAbABhAHMAaAAgAG8AbgAgAHMAdABhAGcAZQAgACAANAANAAoAIABGAGUAZQBkAC0AZgBsAGEAcwBoACAAbwBuACAAcwB0AGEAZwBlACAAMQA2AA0ACgBSAGUAYQBkAGkAbgBnACAAIAAgACAAIAAgACAANQA2ACAAbQBpAGwAbABpAHMAZQBjAG8AbgBkAHMADQAKAFIAdQBuACAAbABlAHYAZQBsADoAIABJAG4AaQB0AGkAYQBsAGkAegBhAHQAaQBvAG4AIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgAA0ACgBSAGUAYQBkAGkAbgBnACAAaQBuAGkAdABpAGEAbAAgAHQAZQBtAHAAZQByAGEAdAB1AHIAZQAgAHAAcgBvAGYAaQBsAGUAcwANAAoASQBuAGkAdABpAGEAbABpAHoAaQBuAGcAIABmAHIAbwBtACAAbwBsAGQAIAByAGUAcwB1AGwAdABzAA0ACgBSAGUAYQBkAGkAbgBnACAAaQBuAGkAdABpAGEAbAAgAGMAbwBtAHAAbwBzAGkAdABpAG8AbgAgAHAAcgBvAGYAaQBsAGUAcwANAAoASQBuAGkAdABpAGEAbABpAHoAYQB0AGkAbwBuACAAIAAgACAAIAAgACAAIAAwACAAbQBpAGwAbABpAHMAZQBjAG8AbgBkAHMADQAKAFIAdQBuACAAbABlAHYAZQBsADoAIABDAG8AbQBwAGwAZQB0AGUAIABtAG8AZABlAGwAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAANAAoADQAKACAAIAAgACAAIAAgAEkAdABlAHIAYQB0AGkAbwBuACAAIAAgACAAbABvAGcAKABFAHIAcgAvAFQAbwBsACkADQAKACAAIAAgACAAIAAgACAAIAAgADAAIAAgACAAIAAgACAAIAAgACAAIAAgADIALgA2ADcANwA5AA0ACgAgACAAIAAgACAAIAAgACAAIAAxACAAIAAgACAAIAAgACAAIAAgACAALQAwAC4ANQA2ADkAMwANAAoAUwBpAG0AdQBsAGEAdABpAG8AbgAgACAAIAAgACAAIAAgADIAMAAgAG0AaQBsAGwAaQBzAGUAYwBvAG4AZABzAA0ACgBSAHUAbgAgAGwAZQB2AGUAbAA6ACAAUgBlAHAAbwByAHQAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAANAAoAQwBvAG4AdgBlAHIAZwBlAG4AYwBlACAAbwBiAHQAYQBpAG4AZQBkACAAaQBuACAAMQAgAGkAdABlAHIAYQB0AGkAbwBuAHMAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAAgACAAIAANAAoAUgBlAHAAbwByAHQAIAAgACAAIAAgACAAIAAgADkAIABtAGkAbABsAGkAcwBlAGMAbwBuAGQAcwANAAoAQwBhAHAAZQAtAE8AcABlAG4AIABjAGwAZQBhAG4AdQBwACAAYwBhAGwAbABlAGQAIAB3AGkAdABoACAAYwBvAG4AdgBlAHIAZwBlAGQADQAKACAARgBpAHgATQBlAG0AIABkAHIAaQB2AGUAcgAgAGQAbwBuAGUADQAKAA0ACgByAHUAbgAgAHQAaQBtAGUAOgAgADAALgAxADQAIABzAGUAYwBvAG4AZABzAA0ACgAAAOMAAABVAHMAaQBuAGcAOgAgAEMAOgBcAFAAcgBvAGcAcgBhAG0AIABGAGkAbABlAHMAXABDAGgAZQBtAFMAZQBwAEwAOAB2ADQAMABcAGIAaQBuAFwAYwBvAC0AYwBvAGwAMgAuAGUAeABlAA0ACgANAAoAQwBBAFAARQAtAE8AUABFAE4AIAB0AGgAZQByAG0AbwAtAHAAcgBvAHAAZQByAHQAaQBlAHMAIAB3AGUAcgBlACAAZABpAHMAYQBiAGwAZQBkAC4ADQAKAEEAbABsACAAYwBhAGwAYwB1AGwAYQB0AGkAbwBuACAAbQBlAHQAaABvAGQAcwAgAGgAYQB2AGUAIABiAGUAZQBuACAAZABlAHQAZQByAG0AaQBuAGUAZAAgAGIAeQAgAEMAaABlAG0AUwBlAHAALgANAAoAUwBlAGUAIABvAHUAdABwAHUAdAAgAHIAZQBwAG8AcgB0ACAAbwByACAAZwByAGEAcABoAGkAYwBhAGwAIAB1AHMAZQByACAAaQBuAHQAZQByAGYAYQBjAGUAIABmAG8AcgAgAG0AbwByAGUAIABpAG4AZgBvAHIAbQBhAHQAaQBvAG4ALgANAAoAAAAAAAAAAAAAAAAAAAACAAAAEAAAAAAApgINAAAARgBlAGUAZAAxAF8AcwB0AGEAZwBlADEANgAFAAAARgBlAGUAZAAxAAQAAABlAG4ADAAAAEYAZQBlAGQAMgBfAHMAdABhAGcAZQA0AAUAAABGAGUAZQBkADIAAgAAAP//////////CgAAAFQAbwBwAFAAcgBvAGQAdQBjAHQAAwAAAHQAbwBwAAIAAAD//////v///w0AA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W1ldGVyVmFsaWRhdGVkSGFuZGxlcgIAAAAlQ2FwZU9wZW4uUGFyYW1ldGVyVmFsdWVDaGFuZ2VkSGFuZGxlcgIAAAAkQ2FwZU9wZW4uUGFyYW1ldGVyTW9kZUNoYW5nZWRIYW5kbGVyAgAAAB5DYXBlT3Blbi5QYXJhbWV0ZXJSZXNldEhhbmRsZXICAAAAMVN5c3RlbS5Db21wb25lbnRNb2RlbC5Qcm9wZXJ0eUNoYW5nZWRFdmVudEhhbmRsZXInAAAAJENhcGVPcGVuLkNvbXBvbmVudE5hbWVDaGFuZ2VkSGFuZGxlcgIAAAArQ2FwZU9wZW4uQ29tcG9uZW50RGVzY3JpcHRpb25DaGFuZ2VkSGFuZGxlcgIAAACGAAAACYcAAAABAAAAAXj////W////AAAAAAF3////1f///wIAAAABdv///9b///8AAAAACgoKCgoGiwAAABNUZW1wZXJhdHVyZSBwcm9maWxlBowAAAAZVGVtcGVyYXR1cmUgYXQgZWFjaCBzdGFnZQoKCgEWAAAAFQAAAAmNAAAAAQAAAAFy////1v///wAAAAABcf///9X///8CAAAAAXD////W////AAAAAAoKCgoKBpEAAAAQUHJlc3N1cmUgcHJvZmlsZQaSAAAAFlByZXNzdXJlIGF0IGVhY2ggc3RhZ2UKCgoBFwAAABUAAAAJkwAAAAEAAAABbP///9b///8AAAAAAWv////V////AgAAAAFq////1v///wAAAAAKCgoKCgaXAAAAE1ZhcG91ciBGbG93IHByb2ZpbGUGmAAAABlWYXBvdXIgRmxvdyBhdCBlYWNoIHN0YWdlCgoKARgAAAAVAAAACZkAAAABAAAAAWb////W////AAAAAAFl////1f///wIAAAABZP///9b///8AAAAACgoKCgoGnQAAABNMaXF1aWQgRmxvdyBwcm9maWxlBp4AAAAZTGlxdWlkIEZsb3cgYXQgZWFjaCBzdGFnZQoKCgEZAAAAFQAAAAmfAAAAAQAAAAFg////1v///wAAAAABX////9X///8CAAAAAV7////W////AAAAAAoKCgoKBqMAAAAORHV0aWVzIHByb2ZpbGUGpAAAABREdXRpZXMgYXQgZWFjaCBzdGFnZQoKCgEaAAAAFQAAAAmlAAAAAQAAAAFa////1v///wAAAAABWf///9X///8CAAAAAVj////W////AAAAAAoKCgoKBqkAAAAZVmFwb3VyIE1vbGV3ZWlnaHQgcHJvZmlsZQaqAAAAH1ZhcG91ciBNb2xld2VpZ2h0IGF0IGVhY2ggc3RhZ2UKCgoBGwAAABUAAAAJqwAAAAEAAAABVP///9b///8AAAAAAVP////V////AgAAAAFS////1v///wAAAAAKCgoKCgavAAAAFlZhcG91ciBEZW5zaXR5IHByb2ZpbGUGsAAAABxWYXBvdXIgRGVuc2l0eSBhdCBlYWNoIHN0YWdlCgoKARwAAAAVAAAACbEAAAABAAAAAU7////W////AAAAAAFN////1f///wIAAAABTP///9b///8AAAAACgoKCgoGtQAAABhWYXBvdXIgVmlzY29zaXR5IHByb2ZpbGUGtgAAAB5WYXBvdXIgVmlzY29zaXR5IGF0IGVhY2ggc3RhZ2UKCgoBHQAAABUAAAAJtwAAAAEAAAABSP///9b///8AAAAAAUf////V////AgAAAAFG////1v///wAAAAAKCgoKCga7AAAAHFZhcG91ciBIZWF0IGNhcGFjaXR5IHByb2ZpbGUGvAAAACJWYXBvdXIgSGVhdCBjYXBhY2l0eSBhdCBlYWNoIHN0YWdlCgoKAR4AAAAVAAAACb0AAAABAAAAAUL////W////AAAAAAFB////1f///wIAAAABQP///9b///8AAAAACgoKCgoGwQAAABtWYXBvdXIgVGguIENvbmR1Y3QuIHByb2ZpbGUGwgAAACFWYXBvdXIgVGguIENvbmR1Y3QuIGF0IGVhY2ggc3RhZ2UKCgoBHwAAABUAAAAJwwAAAAEAAAABPP///9b///8AAAAAATv////V////AgAAAAE6////1v///wAAAAAKCgoKCgbHAAAAGlZhcG91ciBTdGQgZGVuc2l0eSBwcm9maWxlBsgAAAAgVmFwb3VyIFN0ZCBkZW5zaXR5IGF0IGVhY2ggc3RhZ2UKCgoBIAAAABUAAAAJyQAAAAEAAAABNv///9b///8AAAAAATX////V////AgAAAAE0////1v///wAAAAAKCgoKCgbNAAAAGUxpcXVpZCBNb2xld2VpZ2h0IHByb2ZpbGUGzgAAAB9MaXF1aWQgTW9sZXdlaWdodCBhdCBlYWNoIHN0YWdlCgoKASEAAAAVAAAACc8AAAABAAAAATD////W////AAAAAAEv////1f///wIAAAABLv///9b///8AAAAACgoKCgoG0wAAABZMaXF1aWQgRGVuc2l0eSBwcm9maWxlBtQAAAAcTGlxdWlkIERlbnNpdHkgYXQgZWFjaCBzdGFnZQoKCgEiAAAAFQAAAAnVAAAAAQAAAAEq////1v///wAAAAABKf///9X///8CAAAAASj////W////AAAAAAoKCgoKBtkAAAAYTGlxdWlkIFZpc2Nvc2l0eSBwcm9maWxlBtoAAAAeTGlxdWlkIFZpc2Nvc2l0eSBhdCBlYWNoIHN0YWdlCgoKASMAAAAVAAAACdsAAAABAAAAAST////W////AAAAAAEj////1f///wIAAAABIv///9b///8AAAAACgoKCgoG3wAAABxMaXF1aWQgSGVhdCBjYXBhY2l0eSBwcm9maWxlBuAAAAAiTGlxdWlkIEhlYXQgY2FwYWNpdHkgYXQgZWFjaCBzdGFnZQoKCgEkAAAAFQAAAAnhAAAAAQAAAAEe////1v///wAAAAABHf///9X///8CAAAAARz////W////AAAAAAoKCgoKBuUAAAAbTGlxdWlkIFRoLiBDb25kdWN0LiBwcm9maWxlBuYAAAAhTGlxdWlkIFRoLiBDb25kdWN0LiBhdCBlYWNoIHN0YWdlCgoKASUAAAAVAAAACecAAAABAAAAARj////W////AAAAAAEX////1f///wIAAAABFv///9b///8AAAAACgoKCgoG6wAAABxMaXF1aWQgU3VyZi4gdGVuc2lvbiBwcm9maWxlBuwAAAAiTGlxdWlkIFN1cmYuIHRlbnNpb24gYXQgZWFjaCBzdGFnZQoKCgEmAAAAFQAAAAntAAAAAQAAAAES////1v///wAAAAABEf///9X///8CAAAAARD////W////AAAAAAoKCgoKBvEAAAAaTGlxdWlkIFN0ZCBEZW5zaXR5IHByb2ZpbGUG8gAAACBMaXF1aWQgU3RkIERlbnNpdHkgYXQgZWFjaCBzdGFnZQoKChFcAAAABQAAAAbzAAAABEF1dG8G9AAAAAJUUAb1AAAAA1BWRgb2AAAAAlBIBvcAAAADVFZGEIcAAAAgAAAACAaamZmZmaF0QAgGSOF6FK4TdUAIBvYoXI/CVXVACAaF61G4HmF1QAgGUrgehethdUAIBq5H4XoUYnVACAauR+F6FGJ1QAgGrkfhehRidUAIBq5H4XoUYnVACAauR+F6FGJ1QAgGrkfhehRidUAIBgrXo3A9YnVACAauR+F6FGJ1QAgGCtejcD1idUAIBlK4HoXrYXVACAaPwvUoXGN1QAgGhetRuB6hdUAIBnE9CtejrHVACAZmZmZmZq51QAgGH4XrUbiudUAIBh+F61G4rnVACAYfhetRuK51QAgGH4XrUbiudUAIBh+F61G4rnVACAYfhetRuK51QAgGH4XrUbiudUAIBh+F61G4rnVACAbXo3A9Cq91QAgGPQrXo3CxdUAIBsP1KFyPwnVACAaF61G4Hg11QAgGSOF6FK7XcUAQjQAAACAAAAAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QAgGAAAAANC8+EAIBgAAAADQvPhACAYAAAAA0Lz4QBCTAAAAIAAAAAgGJnrPN1iu7z8IBprtCn2wbAFACAYGQx1WuAUBQAgG3htDAHAMAUAIBkvLSL2nEgJACAZmnlxTIBMCQAgGg4k/ijoTAkAIBsGopE5AEwJACAbNIhRbQRMCQAgG3lm77UITAkAIBqq0xTU+EwJACAZV203wTRMCQAgGM/lmmxsTAkAIBgpkdha9EwJACAbxttJrsxECQAgGZHWr56QXAkAIBt3T1R2LDQJACAY6It+l1EUCQAgGNkHUfQBSAkAIBjjAzHfwUwJACAZrEyf3O1QCQAgG51Hxf0dUAkAIBviImBJJVAJACAbzy2CMSFQCQAgGy6Da4ERUAkAIBsWp1sIsVAJACAYWak3zjlMCQAgGM6DejJpPAkAIBmg8EcR5OAJACAaVgJiEC9kBQAgG9dvXgXOmAUAIBuLqAIi7ugpAEJkAAAAgAAAACAbw9bUuNQLzPwgGwCZr1EM08j8IBnpSJjW0QfI/CAan6h7ZXPX6PwgG6gq2EU/2+j8IBiLhe3+D9vo/CAafH0YIj/b6PwgGqpm1FJD2+j8IBtiBc0aU9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</ParameterData>
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.CapeOpenUO</Type>
+ <ObjectClass>CAPEOPEN</ObjectClass>
+ <EmbeddedImageData></EmbeddedImageData>
+ <UseEmbeddedImage>false</UseEmbeddedImage>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ReactionSetID>DefaultSet</ReactionSetID>
+ <ReactionSetName></ReactionSetName>
+ <RecalcOutputStreams>true</RecalcOutputStreams>
+ <MobileCompatible>false</MobileCompatible>
+ <ProductName>ChemSep Column / Flash</ProductName>
+ <ProductDescription>ChemSep CAPE-OPEN Unit Operation</ProductDescription>
+ <ProductAuthor>Copyright (C) Ross Taylor and Harry Kooijman 2020</ProductAuthor>
+ <ProductContactInfo></ProductContactInfo>
+ <ProductPage>http://www.chemsep.com/</ProductPage>
+ <ProductVersion>2.0.0.10</ProductVersion>
+ <ProductAssembly>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</ProductAssembly>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>CapeOpenUnitOperation</ComponentDescription>
+ <ComponentName>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</ComponentName>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</Name>
<UserDefinedChartNames />
- <ProductName>Stream Mixer</ProductName>
- <ProductDescription>Mixes multiple Material Streams into a single one</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>8.6.5.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
<IsSource>false</IsSource>
<IsSink>false</IsSink>
<DynamicProperties />
@@ -5687,6 +5378,21 @@ <DynamicPropertiesUnitTypes />
<AttachedUtilities />
<PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+ <CAPEOPEN_Object_Info>
+ <Type>DWSIM.UnitOperations.UnitOperations.Auxiliary.CapeOpen.CapeOpenUnitOpInfo</Type>
+ <TypeName>ChemSepUO.ChemSep_UnitOperation.1</TypeName>
+ <Version>2.0.0.10</Version>
+ <Description>ChemSep CAPE-OPEN Unit Operation</Description>
+ <HelpURL></HelpURL>
+ <VendorURL>http://www.chemsep.com/</VendorURL>
+ <AboutInfo>Copyright (C) Ross Taylor and Harry Kooijman 2020</AboutInfo>
+ <CapeVersion>1.0</CapeVersion>
+ <Location>C:\Program Files\ChemSepL8v40\bin\ChemsepUO64.dll</Location>
+ <Name>ChemSep Column / Flash</Name>
+ <ImplementedCategory></ImplementedCategory>
+ </CAPEOPEN_Object_Info>
+ 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</SimulationObject>
<SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
@@ -5695,13 +5401,13 @@ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
<OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
<FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mass</DefinedFlow>
+ <DefinedFlow>Mole</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-166.710668180743</TotalEnergyFlow>
+ <TotalEnergyFlow>-152.355301884039</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-9f510731-7729-4083-8c48-1c157b4ee026</ComponentName>
- <Name2>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name2>
+ <ComponentName>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</ComponentName>
+ <Name2>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
@@ -5721,7 +5427,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:22</LastUpdated>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -5729,7 +5436,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name>
+ <Name>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -5755,20 +5462,20 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.763250971621835</MassFraction>
- <MoleFraction>0.5</MoleFraction>
- <Molarity>11556.5422306546</Molarity>
+ <MassFraction>0.339097855508171</MassFraction>
+ <MoleFraction>0.46842375932563</MoleFraction>
+ <Molarity>4080.10895058824</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1.79548461964337</Kvalue>
- <lnKvalue>0.585274968589596</lnKvalue>
- <MassFlow>0.0212014158783843</MassFlow>
- <MolarFlow>0.365043557435325</MolarFlow>
+ <Kvalue>1.59651400847319</Kvalue>
+ <lnKvalue>0.467822507624142</lnKvalue>
+ <MassFlow>0.021201415549727</MassFlow>
+ <MolarFlow>0.365043551776541</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>5.07429608938772E-05</VolumetricFlow>
- <VolumetricFraction>1.60641972316535</VolumetricFraction>
+ <VolumetricFlow>-0.000147310706761259</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -5780,20 +5487,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.236749028378165</MassFraction>
- <MoleFraction>0.5</MoleFraction>
- <Molarity>11556.5422306546</Molarity>
+ <MassFraction>0.000658881973956092</MassFraction>
+ <MoleFraction>0.0029342739528887</MoleFraction>
+ <Molarity>25.5583906245382</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.204515380356629</Kvalue>
- <lnKvalue>-1.58711209675951</lnKvalue>
- <MassFlow>0.00657636189939347</MassFlow>
- <MolarFlow>0.365043557435325</MolarFlow>
+ <Kvalue>0.291068903902654</Kvalue>
+ <lnKvalue>-1.23419525666872</lnKvalue>
+ <MassFlow>4.11952782984523E-05</MassFlow>
+ <MolarFlow>0.00228668543028209</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>1.24322605779949E-05</VolumetricFlow>
- <VolumetricFraction>0.393580276834651</VolumetricFraction>
+ <VolumetricFlow>2.17832300211711E-07</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -5805,19 +5512,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>0.660243262517873</MassFraction>
+ <MoleFraction>0.52864196672148</MoleFraction>
+ <Molarity>4604.62727847559</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>NaN</Kvalue>
- <lnKvalue>NaN</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <Kvalue>0.475370565054175</Kvalue>
+ <lnKvalue>-0.743660642139997</lnKvalue>
+ <MassFlow>0.0412803901445245</MassFlow>
+ <MolarFlow>0.411971718573726</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFlow>0.000326031013710447</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -5833,27 +5540,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>879.388378247172</density>
- <enthalpy>10.867318406018</enthalpy>
- <entropy>0.0364491645346906</entropy>
+ <density>698.822523077729</density>
+ <enthalpy>92.1275948036861</enthalpy>
+ <entropy>0.278573019143262</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0277777777777778</massflow>
- <molar_enthalpy>413.471145530632</molar_enthalpy>
- <molar_entropy>1.38678901737593</molar_entropy>
- <molarflow>0.730087114870651</molarflow>
- <molecularWeight>38.04721</molecularWeight>
+ <massflow>0.0625230009725499</massflow>
+ <molar_enthalpy>7391.35024207687</molar_enthalpy>
+ <molar_entropy>22.3497721488139</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
+ <molecularWeight>80.2294932134833</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0475505128088451</surfaceTension>
- <temperature>298.15</temperature>
- <thermalConductivity>0.211684674125455</thermalConductivity>
- <volumetric_flow>3.15876107359361E-05</volumetric_flow>
+ <surfaceTension>0.0176602962372999</surfaceTension>
+ <temperature>330.712554600658</temperature>
+ <thermalConductivity>0.120140116612103</thermalConductivity>
+ <volumetric_flow>8.94690696247E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.085641233109552</helmholtz_energy>
- <internal_energy>10.7816771729085</internal_energy>
+ <helmholtz_energy>-0.143992171410602</helmholtz_energy>
+ <internal_energy>91.9836026322755</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
- <molar_internal_energy>410.212735549854</molar_internal_energy>
+ <molar_helmholtz_energy>-11.5524189389816</molar_helmholtz_energy>
+ <molar_internal_energy>7379.79782313789</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -5863,23 +5570,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>1.50165678404913</ActivityCoeff>
+ <ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.763250971621835</MassFraction>
- <MoleFraction>0.5</MoleFraction>
- <Molarity>11556.5422306547</Molarity>
+ <MassFraction>0.339097855508171</MassFraction>
+ <MoleFraction>0.468423759325631</MoleFraction>
+ <Molarity>4080.10895058825</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.454463642386878</FugacityCoeff>
+ <FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0212014158783843</MassFlow>
- <MolarFlow>0.365043557435325</MolarFlow>
+ <MassFlow>0.021201415549727</MassFlow>
+ <MolarFlow>0.365043551776542</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>50662.5</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>2.53714804469386E-05</VolumetricFlow>
- <VolumetricFraction>0.803209861582674</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0775611185695147</PartialVolume>
+ <VolumetricFlow>-7.36553533806294E-05</VolumetricFlow>
+ <VolumetricFraction>-0.82324934963105</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -5888,22 +5595,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.68270859296819</ActivityCoeff>
+ <ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.236749028378165</MassFraction>
- <MoleFraction>0.5</MoleFraction>
- <Molarity>11556.5422306547</Molarity>
+ <MassFraction>0.000658881973956092</MassFraction>
+ <MoleFraction>0.0029342739528887</MoleFraction>
+ <Molarity>25.5583906245382</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0527040783253512</FugacityCoeff>
+ <FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00657636189939347</MassFlow>
- <MolarFlow>0.365043557435325</MolarFlow>
+ <MassFlow>4.11952782984524E-05</MassFlow>
+ <MolarFlow>0.00228668543028209</MolarFlow>
<Name>Water</Name>
- <PartialPressure>50662.5</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>6.21613028899746E-06</VolumetricFlow>
- <VolumetricFraction>0.196790138417326</VolumetricFraction>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0183092386194671</PartialVolume>
+ <VolumetricFlow>1.08916150105856E-07</VolumetricFlow>
+ <VolumetricFraction>0.0012173609333676</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -5913,22 +5620,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.70977396256326</ActivityCoeff>
+ <ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>0.660243262517873</MassFraction>
+ <MoleFraction>0.528641966721481</MoleFraction>
+ <Molarity>4604.6272784756</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.138391181887592</FugacityCoeff>
+ <FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <MassFlow>0.0412803901445245</MassFlow>
+ <MolarFlow>0.411971718573726</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <PartialVolume>0.152105858999627</PartialVolume>
+ <VolumetricFlow>0.000163015506855224</VolumetricFlow>
+ <VolumetricFraction>1.82203198869768</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -5943,29 +5650,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00131450091730295</compressibilityFactor>
- <density>879.388378247172</density>
- <enthalpy>10.867318406018</enthalpy>
- <entropy>0.0364491645346906</entropy>
+ <compressibilityFactor>0.00420157603846687</compressibilityFactor>
+ <density>698.82252307773</density>
+ <enthalpy>92.127594803686</enthalpy>
+ <entropy>0.278573019143262</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>6.85051893836374E-07</kinematic_viscosity>
- <massflow>0.0277777777777778</massflow>
+ <kinematic_viscosity>3.47863247875279E-07</kinematic_viscosity>
+ <massflow>0.06252300097255</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>413.471145530632</molar_enthalpy>
- <molar_entropy>1.38678901737593</molar_entropy>
- <molarflow>0.730087114870651</molarflow>
+ <molar_enthalpy>7391.35024207687</molar_enthalpy>
+ <molar_entropy>22.3497721488139</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>38.04721</molecularWeight>
- <thermalConductivity>0.211684674125455</thermalConductivity>
- <viscosity>0.000602426673935923</viscosity>
- <volumetric_flow>3.15876107359361E-05</volumetric_flow>
+ <molecularWeight>80.2294932134834</molecularWeight>
+ <thermalConductivity>0.120140116612103</thermalConductivity>
+ <viscosity>0.000243094672566216</viscosity>
+ <volumetric_flow>8.94690696247E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.085641233109552</helmholtz_energy>
- <internal_energy>10.7816771729085</internal_energy>
+ <helmholtz_energy>-0.143992171410602</helmholtz_energy>
+ <internal_energy>91.9836026322754</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
- <molar_internal_energy>410.212735549854</molar_internal_energy>
+ <molar_helmholtz_energy>-11.5524189389816</molar_helmholtz_energy>
+ <molar_internal_energy>7379.79782313789</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -5977,8 +5684,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.965873983786056</MassFraction>
- <MoleFraction>0.897742309821686</MoleFraction>
+ <MassFraction>0.632870849725522</MassFraction>
+ <MoleFraction>0.747845093665042</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -5987,11 +5694,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>90963.7395426823</PartialPressure>
- <PartialVolume>26.3206733940236</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>22.9639997463424</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>4.84984668104951E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6002,8 +5709,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0341260162139435</MassFraction>
- <MoleFraction>0.102257690178314</MoleFraction>
+ <MassFraction>0.000224192330752703</MassFraction>
+ <MoleFraction>0.000854075903217424</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -6012,11 +5719,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>10361.2604573177</PartialPressure>
- <PartialVolume>8.16427896456258</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>7.12308903593074</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>2.60083766649725E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6027,8 +5734,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
+ <MassFraction>0.366904957943725</MassFraction>
+ <MoleFraction>0.251300830431741</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -6038,10 +5745,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>45.4101785155212</PartialVolume>
+ <PartialVolume>39.6190216071208</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>2.18884339386236E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6070,23 +5777,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>1.50165678404913</ActivityCoeff>
+ <ActivityCoeff>1.52097490890229</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.763250971621835</MassFraction>
- <MoleFraction>0.5</MoleFraction>
- <Molarity>11556.5422306547</Molarity>
+ <MassFraction>0.339097855508171</MassFraction>
+ <MoleFraction>0.468423759325631</MoleFraction>
+ <Molarity>4080.10895058825</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.454463642386878</FugacityCoeff>
+ <FugacityCoeff>1.59651403743814</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0212014158783843</MassFlow>
- <MolarFlow>0.365043557435325</MolarFlow>
+ <MassFlow>0.021201415549727</MassFlow>
+ <MolarFlow>0.365043551776542</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>50662.5</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>2.53714804469386E-05</VolumetricFlow>
- <VolumetricFraction>0.803209861582674</VolumetricFraction>
- <DiffusionCoefficient>2.98854081321769E-09</DiffusionCoefficient>
+ <PartialPressure>47463.0374136695</PartialPressure>
+ <PartialVolume>-0.0775611185695147</PartialVolume>
+ <VolumetricFlow>-7.36553533806294E-05</VolumetricFlow>
+ <VolumetricFraction>-0.82324934963105</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6095,23 +5802,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.68270859296819</ActivityCoeff>
+ <ActivityCoeff>1.65463658569767</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.236749028378165</MassFraction>
- <MoleFraction>0.5</MoleFraction>
- <Molarity>11556.5422306547</Molarity>
+ <MassFraction>0.000658881973956092</MassFraction>
+ <MoleFraction>0.0029342739528887</MoleFraction>
+ <Molarity>25.5583906245382</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0527040783253512</FugacityCoeff>
+ <FugacityCoeff>0.291068909183409</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.00657636189939347</MassFlow>
- <MolarFlow>0.365043557435325</MolarFlow>
+ <MassFlow>4.11952782984524E-05</MassFlow>
+ <MolarFlow>0.00228668543028209</MolarFlow>
<Name>Water</Name>
- <PartialPressure>50662.5</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>6.21613028899746E-06</VolumetricFlow>
- <VolumetricFraction>0.196790138417326</VolumetricFraction>
- <DiffusionCoefficient>3.87048181574814E-09</DiffusionCoefficient>
+ <PartialPressure>297.315308276448</PartialPressure>
+ <PartialVolume>0.0183092386194671</PartialVolume>
+ <VolumetricFlow>1.08916150105856E-07</VolumetricFlow>
+ <VolumetricFraction>0.0012173609333676</VolumetricFraction>
+ <DiffusionCoefficient>1.05594256255482E-08</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6120,23 +5827,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.70977396256326</ActivityCoeff>
+ <ActivityCoeff>1.48106856659945</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>0.660243262517873</MassFraction>
+ <MoleFraction>0.528641966721481</MoleFraction>
+ <Molarity>4604.6272784756</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.138391181887592</FugacityCoeff>
+ <FugacityCoeff>0.475370573678646</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <MassFlow>0.0412803901445245</MassFlow>
+ <MolarFlow>0.411971718573726</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.60278998872266E-09</DiffusionCoefficient>
+ <PartialPressure>53564.647278054</PartialPressure>
+ <PartialVolume>0.152105858999627</PartialVolume>
+ <VolumetricFlow>0.000163015506855224</VolumetricFlow>
+ <VolumetricFraction>1.82203198869768</VolumetricFraction>
+ <DiffusionCoefficient>6.99153582591128E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6150,36 +5857,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00131450091730295</compressibilityFactor>
- <density>879.388378247172</density>
- <enthalpy>10.867318406018</enthalpy>
- <enthalpyF>-6001.58405450674</enthalpyF>
- <entropy>0.0364491645346906</entropy>
- <entropyF>-12.0421571204103</entropyF>
+ <compressibilityFactor>0.00420157603846687</compressibilityFactor>
+ <density>698.82252307773</density>
+ <enthalpy>92.127594803686</enthalpy>
+ <enthalpyF>-2436.78805422231</enthalpyF>
+ <entropy>0.278573019143262</entropy>
+ <entropyF>-5.08772147773649</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>6.85051893836374E-07</kinematic_viscosity>
- <massflow>0.0277777777777778</massflow>
+ <kinematic_viscosity>3.47863247875279E-07</kinematic_viscosity>
+ <massflow>0.06252300097255</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>413.471145530632</molar_enthalpy>
- <molar_entropy>1.38678901737593</molar_entropy>
- <molarflow>0.730087114870651</molarflow>
+ <molar_enthalpy>7391.35024207687</molar_enthalpy>
+ <molar_entropy>22.3497721488139</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>38.04721</molecularWeight>
+ <molecularWeight>80.2294932134834</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.211684674125455</thermalConductivity>
- <viscosity>0.000602426673935923</viscosity>
- <volumetric_flow>3.15876107359361E-05</volumetric_flow>
- <bulk_modulus>-289.229991511354</bulk_modulus>
+ <thermalConductivity>0.120140116612103</thermalConductivity>
+ <viscosity>0.000243094672566216</viscosity>
+ <volumetric_flow>8.94690696247E-05</volumetric_flow>
+ <bulk_modulus>-14360.6329753624</bulk_modulus>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.085641233109552</helmholtz_energy>
- <internal_energy>10.7816771729085</internal_energy>
- <isothermal_compressibility>-0.00345745610534565</isothermal_compressibility>
+ <helmholtz_energy>-0.143992171410602</helmholtz_energy>
+ <internal_energy>91.9836026322754</internal_energy>
+ <isothermal_compressibility>-6.96348135709363E-05</isothermal_compressibility>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.25840998077808</molar_helmholtz_energy>
- <molar_internal_energy>410.212735549854</molar_internal_energy>
- <idealGasHeatCapacityCp>1.42364663566974</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.18132337598044</idealGasHeatCapacityRatio>
+ <molar_helmholtz_energy>-11.5524189389816</molar_helmholtz_energy>
+ <molar_internal_energy>7379.79782313789</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.65265554124474</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.06689855777933</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -6201,11 +5908,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0775611185695147</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6226,8 +5933,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0183092386194671</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6251,8 +5958,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.152105858999627</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6286,8 +5993,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -6297,10 +6002,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialVolume>-0.0775611185695147</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6311,8 +6016,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -6322,7 +6025,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialVolume>0.0183092386194671</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6336,8 +6039,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -6347,7 +6048,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialVolume>0.152105858999627</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6381,8 +6082,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -6392,10 +6091,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialVolume>-0.0775611185695147</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6406,8 +6105,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -6417,7 +6114,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialVolume>0.0183092386194671</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6431,8 +6128,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -6442,7 +6137,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialVolume>0.152105858999627</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6487,10 +6182,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialVolume>-0.0775611185695147</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6512,7 +6207,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialVolume>0.0183092386194671</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6537,7 +6232,7 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialVolume>0.152105858999627</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -6565,19 +6260,66 @@ </Phases>
</SimulationObject>
<SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</ComponentName>
+ <EnergyFlow>8.60745067063185</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name2>
+ <code>0</code>
+ <IsDirty>false</IsDirty>
+ <CanUsePreviousResults>true</CanUsePreviousResults>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name>
+ <UserDefinedChartNames />
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.6.5.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
<ObjectClass>Streams</ObjectClass>
<SupportsDynamicMode>true</SupportsDynamicMode>
<HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
<OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
<FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mass</DefinedFlow>
+ <DefinedFlow>Mole</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-152.408889853537</TotalEnergyFlow>
- <AtEquilibrium>false</AtEquilibrium>
+ <TotalEnergyFlow>-160.522542219782</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-db971471-1e8a-42d3-ad06-be461cacea57</ComponentName>
- <Name2>MAT-db971471-1e8a-42d3-ad06-be461cacea57</Name2>
+ <ComponentName>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</ComponentName>
+ <Name2>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
@@ -6597,7 +6339,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:22</LastUpdated>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -6605,7 +6348,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-db971471-1e8a-42d3-ad06-be461cacea57</Name>
+ <Name>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -6631,19 +6374,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.85079554049368E-10</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.78953764686614E-12</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>48.9654943370213</Kvalue>
- <lnKvalue>3.87923823348358</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <Kvalue>22.3088875405438</Kvalue>
+ <lnKvalue>3.10498514348734</lnKvalue>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>2.25058744836356E-18</VolumetricFlow>
+ <VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -6656,19 +6399,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>6092.77376946324</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>6635.93672309629</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0.540969372119056</Kvalue>
- <lnKvalue>-0.620848925688731</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <Kvalue>0.869234591855049</Kvalue>
+ <lnKvalue>-0.140142234043564</lnKvalue>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>1.17847174288279E-05</VolumetricFlow>
+ <VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -6681,19 +6424,19 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6910.68370137748</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6396.97971174553</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1.40470232610445</Kvalue>
- <lnKvalue>0.333369102305117</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <Kvalue>1.13565010569385</Kvalue>
+ <lnKvalue>0.127205267304322</lnKvalue>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0.000108209266828059</VolumetricFlow>
+ <VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -6709,27 +6452,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>802.227353678979</density>
- <enthalpy>0.1263045937633</enthalpy>
- <entropy>0.000423627683257757</entropy>
+ <density>760.538419205188</density>
+ <enthalpy>189.397669578096</enthalpy>
+ <entropy>0.512930296717088</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0481312282239006</massflow>
- <molar_enthalpy>7.79215837322055</molar_enthalpy>
- <molar_entropy>0.0261350272454152</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
- <molecularWeight>61.6933885067027</molecularWeight>
+ <massflow>0.0454763199392864</massflow>
+ <molar_enthalpy>11052.3385108945</molar_enthalpy>
+ <molar_entropy>29.9321490303407</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
+ <molecularWeight>58.3551980101696</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0440259158385757</surfaceTension>
- <temperature>298.15</temperature>
- <thermalConductivity>0.139308428645295</thermalConductivity>
- <volumetric_flow>5.99969921284445E-05</volumetric_flow>
+ <surfaceTension>0.0366196444406694</surfaceTension>
+ <temperature>369.246407923844</temperature>
+ <thermalConductivity>0.124396242068209</thermalConductivity>
+ <volumetric_flow>5.97949015998589E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.060170843288607</helmholtz_energy>
- <internal_energy>0.0661337504746934</internal_energy>
+ <helmholtz_energy>-0.0656011746042964</helmholtz_energy>
+ <internal_energy>189.332068403492</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
- <molar_internal_energy>4.08001516144059</molar_internal_energy>
+ <molar_helmholtz_energy>-3.82816953373342</molar_helmholtz_energy>
+ <molar_internal_energy>11048.5103413607</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -6741,21 +6484,21 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.85079554049368E-10</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.78953764686614E-12</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>1.12529372418178E-18</VolumetricFlow>
- <VolumetricFraction>1.87558356554391E-14</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <PartialVolume>-0.0830425260669983</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6766,20 +6509,20 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>6092.77376946324</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>6635.93672309629</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>5.89235871441393E-06</VolumetricFlow>
- <VolumetricFraction>0.0982109020032083</VolumetricFraction>
+ <PartialVolume>0.0187458798832016</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -6791,21 +6534,21 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6910.68370137748</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6396.97971174553</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>5.41046334140295E-05</VolumetricFlow>
- <VolumetricFraction>0.901789097996773</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <PartialVolume>-0.160243016598611</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6819,29 +6562,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00149754502528238</compressibilityFactor>
- <density>802.227353678979</density>
- <enthalpy>0.1263045937633</enthalpy>
- <entropy>0.000423627683257757</entropy>
+ <compressibilityFactor>0.00124699543416998</compressibilityFactor>
+ <density>760.538419205188</density>
+ <enthalpy>189.397669578096</enthalpy>
+ <entropy>0.512930296717088</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>7.54356581787694E-07</kinematic_viscosity>
- <massflow>0.0481312282239006</massflow>
+ <kinematic_viscosity>3.12096171226537E-07</kinematic_viscosity>
+ <massflow>0.0454763199392864</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>7.79215837322055</molar_enthalpy>
- <molar_entropy>0.0261350272454152</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <molar_enthalpy>11052.3385108945</molar_enthalpy>
+ <molar_entropy>29.9321490303407</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>61.6933885067027</molecularWeight>
- <thermalConductivity>0.139308428645295</thermalConductivity>
- <viscosity>0.000605165484337862</viscosity>
- <volumetric_flow>5.99969921284445E-05</volumetric_flow>
+ <molecularWeight>58.3551980101696</molecularWeight>
+ <thermalConductivity>0.124396242068209</thermalConductivity>
+ <viscosity>0.000237361128704622</viscosity>
+ <volumetric_flow>5.97949015998589E-05</volumetric_flow>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.060170843288607</helmholtz_energy>
- <internal_energy>0.0661337504746934</internal_energy>
+ <helmholtz_energy>-0.0656011746042964</helmholtz_energy>
+ <internal_energy>189.332068403492</internal_energy>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
- <molar_internal_energy>4.08001516144059</molar_internal_energy>
+ <molar_helmholtz_energy>-3.82816953373342</molar_helmholtz_energy>
+ <molar_internal_energy>11048.5103413607</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -6853,8 +6596,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>7.8552689004154E-13</MassFraction>
- <MoleFraction>1.07348844110935E-12</MoleFraction>
+ <MassFraction>2.78734523944285E-15</MassFraction>
+ <MoleFraction>3.06321262114274E-15</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -6863,11 +6606,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>1.08771216295405E-07</PartialPressure>
- <PartialVolume>17.9016023256588</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>27.569145645241</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>5.88156369103181E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6878,8 +6621,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0575325219578357</MassFraction>
- <MoleFraction>0.253471356208221</MoleFraction>
+ <MassFraction>0.124920032038696</MassFraction>
+ <MoleFraction>0.442585953643962</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -6888,11 +6631,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>25682.985167798</PartialPressure>
- <PartialVolume>5.55280912123346</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>8.55153637191938</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
+ <DiffusionCoefficient>3.15411875705477E-10</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6903,8 +6646,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.942467478041379</MassFraction>
- <MoleFraction>0.746528643790706</MoleFraction>
+ <MassFraction>0.875079967961301</MassFraction>
+ <MoleFraction>0.557414046356035</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -6913,11 +6656,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>75642.0148320932</PartialPressure>
- <PartialVolume>30.8850364560437</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>47.5641259830025</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
+ <DiffusionCoefficient>2.65448016758951E-11</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6937,6 +6680,8 @@ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
<molar_helmholtz_energy>0</molar_helmholtz_energy>
<molar_internal_energy>0</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.96382536092348</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.0631930833244</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -6946,23 +6691,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>9.36609665906765</ActivityCoeff>
+ <ActivityCoeff>6.70841020604819</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>2.06390062054607E-14</MassFraction>
- <MoleFraction>2.1923365742429E-14</MoleFraction>
- <Molarity>2.85079554049368E-10</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.78953764686614E-12</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>2.83456942214845</FugacityCoeff>
+ <FugacityCoeff>22.3088875415966</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>9.93380717989532E-16</MassFlow>
- <MolarFlow>1.71039157602804E-14</MolarFlow>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>2.22138503385162E-09</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>1.12529372418178E-18</VolumetricFlow>
- <VolumetricFraction>1.87558356554391E-14</VolumetricFraction>
- <DiffusionCoefficient>2.99544174340378E-09</DiffusionCoefficient>
+ <PartialPressure>1.39128416095697E-11</PartialPressure>
+ <PartialVolume>-0.0830425260669983</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6971,23 +6716,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00071619041202</ActivityCoeff>
+ <ActivityCoeff>1.00008095435516</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.136822840719863</MassFraction>
- <MoleFraction>0.4685502900383</MoleFraction>
- <Molarity>6092.77376946324</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>6635.93672309629</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0313434094895116</FugacityCoeff>
+ <FugacityCoeff>0.869234591896069</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0065854513729301</MassFlow>
- <MolarFlow>0.36554809988688</MolarFlow>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
- <PartialPressure>47475.8581381307</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>5.89235871441393E-06</VolumetricFlow>
- <VolumetricFraction>0.0982109020032083</VolumetricFraction>
- <DiffusionCoefficient>3.87941926263822E-09</DiffusionCoefficient>
+ <PartialPressure>51591.3910619571</PartialPressure>
+ <PartialVolume>0.0187458798832016</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>1.19050276527809E-08</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -6996,23 +6741,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.00551404572164</ActivityCoeff>
+ <ActivityCoeff>1.00071341890987</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.863177159280117</MassFraction>
- <MoleFraction>0.53144970996168</MoleFraction>
- <Molarity>6910.68370137748</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6396.97971174553</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0813875285498997</FugacityCoeff>
+ <FugacityCoeff>1.13565010574745</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0415457768509695</MassFlow>
- <MolarFlow>0.414620235633715</MolarFlow>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>53849.1418618672</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>5.41046334140295E-05</VolumetricFlow>
- <VolumetricFraction>0.901789097996773</VolumetricFraction>
- <DiffusionCoefficient>2.6088001699863E-09</DiffusionCoefficient>
+ <PartialPressure>49733.6089380429</PartialPressure>
+ <PartialVolume>-0.160243016598611</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7026,36 +6771,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00149754502528238</compressibilityFactor>
- <density>802.227353678979</density>
- <enthalpy>0.1263045937633</enthalpy>
- <enthalpyF>-3484.59544673195</enthalpyF>
- <entropy>0.000423627683257757</entropy>
- <entropyF>0.000423627682931141</entropyF>
+ <compressibilityFactor>0.00124699543416998</compressibilityFactor>
+ <density>760.538419205188</density>
+ <enthalpy>189.397669578096</enthalpy>
+ <enthalpyF>-3529.80501575521</enthalpyF>
+ <entropy>0.512930296717088</entropy>
+ <entropyF>0.512930296717086</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>7.54356581787694E-07</kinematic_viscosity>
- <massflow>0.0481312282239006</massflow>
+ <kinematic_viscosity>3.12096171226537E-07</kinematic_viscosity>
+ <massflow>0.0454763199392864</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>7.79215837322055</molar_enthalpy>
- <molar_entropy>0.0261350272454152</molar_entropy>
- <molarflow>0.78016833552061</molarflow>
+ <molar_enthalpy>11052.3385108945</molar_enthalpy>
+ <molar_entropy>29.9321490303407</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>61.6933885067027</molecularWeight>
+ <molecularWeight>58.3551980101696</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.139308428645295</thermalConductivity>
- <viscosity>0.000605165484337862</viscosity>
- <volumetric_flow>5.99969921284445E-05</volumetric_flow>
- <bulk_modulus>-90.8938782184429</bulk_modulus>
+ <thermalConductivity>0.124396242068209</thermalConductivity>
+ <viscosity>0.000237361128704622</viscosity>
+ <volumetric_flow>5.97949015998589E-05</volumetric_flow>
+ <bulk_modulus>-96.909078489638</bulk_modulus>
<gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.060170843288607</helmholtz_energy>
- <internal_energy>0.0661337504746934</internal_energy>
- <isothermal_compressibility>-0.0110018410436479</isothermal_compressibility>
+ <helmholtz_energy>-0.0656011746042964</helmholtz_energy>
+ <internal_energy>189.332068403492</internal_energy>
+ <isothermal_compressibility>-0.010318950665772</isothermal_compressibility>
<molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-3.71214321177996</molar_helmholtz_energy>
- <molar_internal_energy>4.08001516144059</molar_internal_energy>
- <idealGasHeatCapacityCp>1.66460606324854</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.08808958782905</idealGasHeatCapacityRatio>
+ <molar_helmholtz_energy>-3.82816953373342</molar_helmholtz_energy>
+ <molar_internal_energy>11048.5103413607</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.96129767676082</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.07833204615019</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -7077,11 +6822,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.0830425260669983</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7102,8 +6847,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0.0187458798832016</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -7127,11 +6872,11 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>-0.160243016598611</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7162,8 +6907,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -7173,10 +6916,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialVolume>-0.0830425260669983</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7187,8 +6930,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -7198,7 +6939,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialVolume>0.0187458798832016</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -7212,8 +6953,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -7223,10 +6962,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialVolume>-0.160243016598611</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7257,8 +6996,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -7268,10 +7005,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialVolume>-0.0830425260669983</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7282,8 +7019,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -7293,7 +7028,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialVolume>0.0187458798832016</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -7307,8 +7042,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -7318,10 +7051,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialVolume>-0.160243016598611</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7363,10 +7096,10 @@ <MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0737984191993252</PartialVolume>
+ <PartialVolume>-0.0830425260669983</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7388,7 +7121,7 @@ <MolarFlow>0</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.0180809547091451</PartialVolume>
+ <PartialVolume>0.0187458798832016</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
@@ -7413,10 +7146,10 @@ <MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
- <PartialVolume>0.146372899520274</PartialVolume>
+ <PartialVolume>-0.160243016598611</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7441,6 +7174,137 @@ </Phases>
</SimulationObject>
<SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Cooler</Type>
+ <ObjectClass>Exchangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
+ <OutletTemperature>298.15</OutletTemperature>
+ <OutletVaporFraction>0</OutletVaporFraction>
+ <CalcMode>OutletTemperature</CalcMode>
+ <Eficiencia>100</Eficiencia>
+ <DeltaT>-71.0964079238436</DeltaT>
+ <DeltaQ>8.60745067063185</DeltaQ>
+ <MobileCompatible>true</MobileCompatible>
+ <ExternalSolverID></ExternalSolverID>
+ <ExternalSolverConfigData></ExternalSolverConfigData>
+ <ComponentDescription>Resfriador</ComponentDescription>
+ <ComponentName>RESF-26c14620-b257-493a-b6d0-b997b40f8564</ComponentName>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>RESF-26c14620-b257-493a-b6d0-b997b40f8564</Name>
+ <UserDefinedChartNames />
+ <ProductName>Cooler</ProductName>
+ <ProductDescription>Simple cooler model</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.6.5.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>1.0</Data>
+ </Property>
+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>1.0</Data>
+ </Property>
+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>101325.0</Data>
+ </Property>
+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>-1.0</Data>
+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Double</PropertyType>
+ <Data>0.0</Data>
+ </Property>
+ </DynamicProperties>
+ <DynamicPropertiesDescriptions>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
+ </Property>
+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Cooler Volume"</Data>
+ </Property>
+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
+ </Property>
+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.String</PropertyType>
+ <Data>"Empties the volume content on the next run."</Data>
+ </Property>
+ </DynamicPropertiesDescriptions>
+ <DynamicPropertiesUnitTypes>
+ <Property>
+ <Name>Flow Conductance</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>67</Data>
+ </Property>
+ <Property>
+ <Name>Volume</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>63</Data>
+ </Property>
+ <Property>
+ <Name>Minimum Pressure</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>46</Data>
+ </Property>
+ <Property>
+ <Name>Initialize using Inlet Stream</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>66</Data>
+ </Property>
+ <Property>
+ <Name>Reset Content</Name>
+ <PropertyType>System.Int64</PropertyType>
+ <Data>66</Data>
+ </Property>
+ </DynamicPropertiesUnitTypes>
+ <AttachedUtilities />
+ <PropertyPackage>PP-caa4e8e0-a63c-4975-a79b-f8a06e7a4f6b</PropertyPackage>
+ </SimulationObject>
+ <SimulationObject>
<Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
<ObjectClass>Streams</ObjectClass>
<SupportsDynamicMode>true</SupportsDynamicMode>
@@ -7449,11 +7313,11 @@ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
<DefinedFlow>Mass</DefinedFlow>
<ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-79.5539552876326</TotalEnergyFlow>
+ <TotalEnergyFlow>-169.129992890414</TotalEnergyFlow>
<AtEquilibrium>true</AtEquilibrium>
<ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</ComponentName>
- <Name2>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</Name2>
+ <ComponentName>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</ComponentName>
+ <Name2>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name2>
<code>0</code>
<InputComposition />
<IsElectrolyteStream>false</IsElectrolyteStream>
@@ -7473,7 +7337,8 @@ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
<Calculated>true</Calculated>
<DebugMode>false</DebugMode>
- <LastUpdated>11/12/2023 02:00:22</LastUpdated>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
<Annotation></Annotation>
<IsAdjustAttached>false</IsAdjustAttached>
<AttachedAdjustId></AttachedAdjustId>
@@ -7481,7 +7346,7 @@ <IsSpecAttached>false</IsSpecAttached>
<AttachedSpecId></AttachedSpecId>
<SpecVarType>Source</SpecVarType>
- <Name>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</Name>
+ <Name>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name>
<UserDefinedChartNames />
<ProductName>Material Stream</ProductName>
<ProductDescription>Contains information about compounds flowing at specified state conditions</ProductDescription>
@@ -7507,19 +7372,19 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.91616119531264E-12</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>NaN</Kvalue>
- <lnKvalue>NaN</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <Kvalue>52.3072770616318</Kvalue>
+ <lnKvalue>3.95713550214948</lnKvalue>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFlow>1.39634210549945E-20</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -7532,19 +7397,19 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>7105.48027062453</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>NaN</Kvalue>
- <lnKvalue>NaN</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <Kvalue>0.560637879120848</Kvalue>
+ <lnKvalue>-0.578680073642136</lnKvalue>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFlow>1.26860824662199E-05</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
@@ -7557,20 +7422,20 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1</MassFraction>
- <MoleFraction>1</MoleFraction>
- <Molarity>6832.55660172031</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6849.61521335677</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
- <Kvalue>1</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0.0416666666666667</MassFlow>
- <MolarFlow>0.415826696739253</MolarFlow>
+ <Kvalue>1.45577434415276</Kvalue>
+ <lnKvalue>0.37553795435176</lnKvalue>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0</PartialVolume>
- <VolumetricFlow>0.000121719210239563</VolumetricFlow>
- <VolumetricFraction>2</VolumetricFraction>
+ <VolumetricFlow>9.90010008181747E-05</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -7585,27 +7450,27 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>684.635836605579</density>
- <enthalpy>0.147998387730284</enthalpy>
- <entropy>0.000496389024753595</entropy>
+ <density>814.352360218552</density>
+ <enthalpy>0.12442402693214</enthalpy>
+ <entropy>0.00041732023119953</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <massflow>0.0416666666666667</massflow>
- <molar_enthalpy>14.8297344473499</molar_enthalpy>
- <molar_entropy>0.0497391730583597</molar_entropy>
- <molarflow>0.415826696739253</molarflow>
- <molecularWeight>100.202</molecularWeight>
+ <massflow>0.0454763199392864</massflow>
+ <molar_enthalpy>7.2607887288477</molar_enthalpy>
+ <molar_entropy>0.0243528047252983</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
+ <molecularWeight>58.3551980101696</molecularWeight>
<pressure>101325</pressure>
- <surfaceTension>0.0193054358083515</surfaceTension>
+ <surfaceTension>0.0461688565551219</surfaceTension>
<temperature>298.15</temperature>
- <thermalConductivity>0.118010205685203</thermalConductivity>
- <volumetric_flow>6.08596051197813E-05</volumetric_flow>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.147992905281822</helmholtz_energy>
- <internal_energy>5.4824484624072E-06</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
- <molar_internal_energy>0.000549352300830126</molar_internal_energy>
+ <thermalConductivity>0.143299726742525</thermalConductivity>
+ <volumetric_flow>5.58435416421973E-05</volumetric_flow>
+ <gibbs_free_energy>1.38777878078145E-17</gibbs_free_energy>
+ <helmholtz_energy>-0.0599408772157934</helmholtz_energy>
+ <internal_energy>0.0644831497163465</internal_energy>
+ <molar_gibbs_free_energy>8.0984105546813E-16</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-3.49786175883089</molar_helmholtz_energy>
+ <molar_internal_energy>3.76292697001681</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -7615,22 +7480,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>7.17641923898794</ActivityCoeff>
+ <ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.91616119531264E-12</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>2.17188219124978</FugacityCoeff>
+ <FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <VolumetricFlow>6.98171052749727E-21</VolumetricFlow>
+ <VolumetricFraction>1.25022703112756E-16</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -7640,22 +7505,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00071619041225</ActivityCoeff>
+ <ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>7105.48027062453</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0313434094895189</FugacityCoeff>
+ <FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
<PartialPressure>0</PartialPressure>
<PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
+ <VolumetricFlow>6.34304123310997E-06</VolumetricFlow>
+ <VolumetricFraction>0.113585941123708</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -7665,22 +7530,22 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.00551404572158</ActivityCoeff>
+ <ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1</MassFraction>
- <MoleFraction>1</MoleFraction>
- <Molarity>6832.55660172031</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6849.61521335677</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0813875285498942</FugacityCoeff>
+ <FugacityCoeff>0</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0416666666666667</MassFlow>
- <MolarFlow>0.415826696739253</MolarFlow>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>101325</PartialPressure>
+ <PartialPressure>0</PartialPressure>
<PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>6.08596051197813E-05</VolumetricFlow>
- <VolumetricFraction>1</VolumetricFraction>
+ <VolumetricFlow>4.95005004090874E-05</VolumetricFlow>
+ <VolumetricFraction>0.886414058876292</VolumetricFraction>
<DiffusionCoefficient>Infinity</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
@@ -7695,29 +7560,29 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00598235873487061</compressibilityFactor>
- <density>684.635836605579</density>
- <enthalpy>0.147998387730284</enthalpy>
- <entropy>0.000496389024753595</entropy>
+ <compressibilityFactor>0.00141110005116182</compressibilityFactor>
+ <density>814.352360218552</density>
+ <enthalpy>0.12442402693214</enthalpy>
+ <entropy>0.00041732023119953</entropy>
<heatCapacityCp>0</heatCapacityCp>
<heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>5.07314344208017E-07</kinematic_viscosity>
- <massflow>0.0416666666666667</massflow>
+ <kinematic_viscosity>7.70571617225547E-07</kinematic_viscosity>
+ <massflow>0.0454763199392864</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>14.8297344473499</molar_enthalpy>
- <molar_entropy>0.0497391730583597</molar_entropy>
- <molarflow>0.415826696739253</molarflow>
+ <molar_enthalpy>7.2607887288477</molar_enthalpy>
+ <molar_entropy>0.0243528047252983</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>100.202</molecularWeight>
- <thermalConductivity>0.118010205685203</thermalConductivity>
- <viscosity>0.000347325580468866</viscosity>
- <volumetric_flow>6.08596051197813E-05</volumetric_flow>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.147992905281822</helmholtz_energy>
- <internal_energy>5.4824484624072E-06</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
- <molar_internal_energy>0.000549352300830126</molar_internal_energy>
+ <molecularWeight>58.3551980101696</molecularWeight>
+ <thermalConductivity>0.143299726742525</thermalConductivity>
+ <viscosity>0.000627516815205051</viscosity>
+ <volumetric_flow>5.58435416421973E-05</volumetric_flow>
+ <gibbs_free_energy>1.38777878078145E-17</gibbs_free_energy>
+ <helmholtz_energy>-0.0599408772157934</helmholtz_energy>
+ <internal_energy>0.0644831497163465</internal_energy>
+ <molar_gibbs_free_energy>8.0984105546813E-16</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-3.49786175883089</molar_helmholtz_energy>
+ <molar_internal_energy>3.76292697001681</molar_internal_energy>
</Properties>
</Phase>
<Phase>
@@ -7729,8 +7594,8 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
+ <MassFraction>5.43567536296924E-15</MassFraction>
+ <MoleFraction>7.18226361496533E-15</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -7739,8 +7604,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>14.1798621355377</PartialVolume>
+ <PartialPressure>7.27742860786362E-10</PartialPressure>
+ <PartialVolume>18.5148582516745</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>4.04529539210131E-11</DiffusionCoefficient>
@@ -7754,8 +7619,8 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
+ <MassFraction>0.0670125388927785</MassFraction>
+ <MoleFraction>0.2854585548075</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -7764,8 +7629,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>4.39838101482063</PartialVolume>
+ <PartialPressure>28924.0880658699</PartialPressure>
+ <PartialVolume>5.74303193133071</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>2.16937922367642E-10</DiffusionCoefficient>
@@ -7779,8 +7644,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1</MassFraction>
- <MoleFraction>1</MoleFraction>
+ <MassFraction>0.932987461107216</MassFraction>
+ <MoleFraction>0.714541445192493</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -7789,8 +7654,8 @@ <MassFlow>0</MassFlow>
<MolarFlow>0</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>101325</PartialPressure>
- <PartialVolume>24.4640424377005</PartialVolume>
+ <PartialPressure>72400.9119341294</PartialPressure>
+ <PartialVolume>31.9430664182405</PartialVolume>
<VolumetricFlow>0</VolumetricFlow>
<VolumetricFraction>0</VolumetricFraction>
<DiffusionCoefficient>1.82573154937481E-11</DiffusionCoefficient>
@@ -7822,23 +7687,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Acetone</ComponentName>
- <ActivityCoeff>7.17641923898794</ActivityCoeff>
+ <ActivityCoeff>9.65375432670081</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>1.36659509767078E-16</MassFraction>
+ <MoleFraction>1.3730907090619E-16</MoleFraction>
+ <Molarity>1.91616119531264E-12</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>2.17188219124978</FugacityCoeff>
+ <FugacityCoeff>2.92162656648511</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <MassFlow>6.21477158891367E-18</MassFlow>
+ <MolarFlow>1.07005227503604E-16</MolarFlow>
<Name>Acetone</Name>
- <PartialPressure>0</PartialPressure>
+ <PartialPressure>1.39128416095697E-11</PartialPressure>
<PartialVolume>0.0737984191993252</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>5.18354190784942E-09</DiffusionCoefficient>
+ <VolumetricFlow>6.98171052749727E-21</VolumetricFlow>
+ <VolumetricFraction>1.25022703112756E-16</VolumetricFraction>
+ <DiffusionCoefficient>2.86904933605675E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7847,23 +7712,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>Water</ComponentName>
- <ActivityCoeff>1.00071619041225</ActivityCoeff>
+ <ActivityCoeff>1.00071619041199</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
+ <MassFraction>0.157188979688624</MassFraction>
+ <MoleFraction>0.5091674420129</MoleFraction>
+ <Molarity>7105.48027062453</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0313434094895189</FugacityCoeff>
+ <FugacityCoeff>0.0313434094895109</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
+ <MassFlow>0.00714837633124984</MassFlow>
+ <MolarFlow>0.396795183380433</MolarFlow>
<Name>Water</Name>
- <PartialPressure>0</PartialPressure>
+ <PartialPressure>51591.3910619571</PartialPressure>
<PartialVolume>0.0180809547091451</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>6.71324433876425E-09</DiffusionCoefficient>
+ <VolumetricFlow>6.34304123310997E-06</VolumetricFlow>
+ <VolumetricFraction>0.113585941123708</VolumetricFraction>
+ <DiffusionCoefficient>3.71572749971442E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7872,23 +7737,23 @@ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
<ComponentDescription></ComponentDescription>
<ComponentName>3-methylhexane</ComponentName>
- <ActivityCoeff>1.00551404572158</ActivityCoeff>
+ <ActivityCoeff>1.00551404572167</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1</MassFraction>
- <MoleFraction>1</MoleFraction>
- <Molarity>6832.55660172031</Molarity>
+ <MassFraction>0.842811020311376</MassFraction>
+ <MoleFraction>0.4908325579871</MoleFraction>
+ <Molarity>6849.61521335677</Molarity>
<Molality>0</Molality>
- <FugacityCoeff>0.0813875285498942</FugacityCoeff>
+ <FugacityCoeff>0.0813875285499013</FugacityCoeff>
<Kvalue>0</Kvalue>
<lnKvalue>0</lnKvalue>
- <MassFlow>0.0416666666666667</MassFlow>
- <MolarFlow>0.415826696739253</MolarFlow>
+ <MassFlow>0.0383279436080366</MassFlow>
+ <MolarFlow>0.382506772400117</MolarFlow>
<Name>3-methylhexane</Name>
- <PartialPressure>101325</PartialPressure>
+ <PartialPressure>49733.6089380429</PartialPressure>
<PartialVolume>0.146372899520274</PartialVolume>
- <VolumetricFlow>6.08596051197813E-05</VolumetricFlow>
- <VolumetricFraction>1</VolumetricFraction>
- <DiffusionCoefficient>4.51446770417322E-09</DiffusionCoefficient>
+ <VolumetricFlow>4.95005004090874E-05</VolumetricFlow>
+ <VolumetricFraction>0.886414058876292</VolumetricFraction>
+ <DiffusionCoefficient>2.49872207065487E-09</DiffusionCoefficient>
<EnthalpyF_Dmol>0</EnthalpyF_Dmol>
<EntropyF_Dmol>0</EntropyF_Dmol>
<DynamicProperties />
@@ -7902,36 +7767,36 @@ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
<Properties>
<Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <compressibilityFactor>0.00598235873487061</compressibilityFactor>
- <density>684.635836605579</density>
- <enthalpy>0.147998387730284</enthalpy>
- <enthalpyF>-1909.29492690318</enthalpyF>
- <entropy>0.000496389024753595</entropy>
- <entropyF>0.000496389024753595</entropyF>
+ <compressibilityFactor>0.00141110005116182</compressibilityFactor>
+ <density>814.352360218552</density>
+ <enthalpy>0.12442402693214</enthalpy>
+ <enthalpyF>-3719.07826130637</enthalpyF>
+ <entropy>0.00041732023119953</entropy>
+ <entropyF>0.000417320231197368</entropyF>
<heatCapacityCp>0</heatCapacityCp>
<jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>5.07314344208017E-07</kinematic_viscosity>
- <massflow>0.0416666666666667</massflow>
+ <kinematic_viscosity>7.70571617225547E-07</kinematic_viscosity>
+ <massflow>0.0454763199392864</massflow>
<massfraction>1</massfraction>
- <molar_enthalpy>14.8297344473499</molar_enthalpy>
- <molar_entropy>0.0497391730583597</molar_entropy>
- <molarflow>0.415826696739253</molarflow>
+ <molar_enthalpy>7.2607887288477</molar_enthalpy>
+ <molar_entropy>0.0243528047252983</molar_entropy>
+ <molarflow>0.77930195578055</molarflow>
<molarfraction>1</molarfraction>
- <molecularWeight>100.202</molecularWeight>
+ <molecularWeight>58.3551980101696</molecularWeight>
<speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.118010205685203</thermalConductivity>
- <viscosity>0.000347325580468866</viscosity>
- <volumetric_flow>6.08596051197813E-05</volumetric_flow>
- <bulk_modulus>-2709104.05471673</bulk_modulus>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>-0.147992905281822</helmholtz_energy>
- <internal_energy>5.4824484624072E-06</internal_energy>
- <isothermal_compressibility>-3.69125725628343E-07</isothermal_compressibility>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-14.8291850950491</molar_helmholtz_energy>
- <molar_internal_energy>0.000549352300830126</molar_internal_energy>
- <idealGasHeatCapacityCp>1.63261361609135</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.05354297154205</idealGasHeatCapacityRatio>
+ <thermalConductivity>0.143299726742525</thermalConductivity>
+ <viscosity>0.000627516815205051</viscosity>
+ <volumetric_flow>5.58435416421973E-05</volumetric_flow>
+ <bulk_modulus>-92.8642458102608</bulk_modulus>
+ <gibbs_free_energy>1.38777878078145E-17</gibbs_free_energy>
+ <helmholtz_energy>-0.0599408772157934</helmholtz_energy>
+ <internal_energy>0.0644831497163465</internal_energy>
+ <isothermal_compressibility>-0.0107684070577948</isothermal_compressibility>
+ <molar_gibbs_free_energy>8.0984105546813E-16</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-3.49786175883089</molar_helmholtz_energy>
+ <molar_internal_energy>3.76292697001681</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.66936815283335</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.09330846846733</idealGasHeatCapacityRatio>
</Properties>
</Phase>
<Phase>
@@ -8038,8 +7903,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -8063,8 +7926,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -8088,8 +7949,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -8133,8 +7992,6 @@ <ComponentName>Acetone</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -8158,8 +8015,6 @@ <ComponentName>Water</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -8183,8 +8038,6 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>0</FugacityCoeff>
@@ -8278,8 +8131,8 @@ <ComponentName>3-methylhexane</ComponentName>
<ActivityCoeff>0</ActivityCoeff>
<PetroleumFraction>false</PetroleumFraction>
- <MassFraction>1</MassFraction>
- <MoleFraction>1</MoleFraction>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
<Molarity>0</Molarity>
<Molality>0</Molality>
<FugacityCoeff>1</FugacityCoeff>
@@ -8316,6 +8169,82 @@ </Phase>
</Phases>
</SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.SpecialOps.Recycle</Type>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <Converged>true</Converged>
+ <CopyOnStreamDataError>false</CopyOnStreamDataError>
+ <Errors>
+ <Item Key="Temperature" Value="0" />
+ <Item Key="Pressure" Value="0" />
+ <Item Key="MassFlow" Value="1.63089128614784E-05" />
+ <Item Key="Enthalpy" Value="-2.52038721174075E-05" />
+ </Errors>
+ <Values>
+ <Item Key="Temperature" Value="298.15" />
+ <Item Key="Pressure" Value="101325" />
+ <Item Key="MassFlow" Value="0.0454600110264249" />
+ <Item Key="Enthalpy" Value="0.124413998992225" />
+ </Values>
+ <IterationsTaken>1</IterationsTaken>
+ <IterationCount>1</IterationCount>
+ <AccelerationMethod>None</AccelerationMethod>
+ <ConvergenceParameters>
+ <Type>DWSIM.UnitOperations.SpecialOps.Helpers.Recycle.ConvergenceParameters</Type>
+ <Temperatura>0.1</Temperatura>
+ <Pressao>0.1</Pressao>
+ <VazaoMassica>0.01</VazaoMassica>
+ <FracaoVapor>0.01</FracaoVapor>
+ <Entalpia>1</Entalpia>
+ <Entropia>0.01</Entropia>
+ <Composicao>0.001</Composicao>
+ </ConvergenceParameters>
+ <ConvergenceHistory>
+ <Type>DWSIM.UnitOperations.SpecialOps.Helpers.Recycle.ConvergenceHistory</Type>
+ </ConvergenceHistory>
+ <MaximumIterations>50</MaximumIterations>
+ <MobileCompatible>true</MobileCompatible>
+ <ObjectClass>Logical</ObjectClass>
+ <IsDirty>true</IsDirty>
+ <CanUsePreviousResults>false</CanUsePreviousResults>
+ <DynamicsSpec>Pressure</DynamicsSpec>
+ <DynamicsOnly>false</DynamicsOnly>
+ <Visible>true</Visible>
+ <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
+ <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
+ <IsFunctional>true</IsFunctional>
+ <ComponentDescription>Reciclo</ComponentDescription>
+ <ComponentName>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</ComponentName>
+ <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
+ <Calculated>true</Calculated>
+ <DebugMode>false</DebugMode>
+ <LastUpdated>04/13/2024 20:24:05</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</Name>
+ <UserDefinedChartNames />
+ <ProductName>Recycle Block</ProductName>
+ <ProductDescription>Block for connecting tear Material Streams</ProductDescription>
+ <ProductAuthor>Daniel Medeiros</ProductAuthor>
+ <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
+ <ProductPage>https://dwsim.inforside.com.br</ProductPage>
+ <ProductVersion>8.6.5.0</ProductVersion>
+ <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
+ <IsSource>false</IsSource>
+ <IsSink>false</IsSink>
+ <DynamicProperties />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <WegPars AccelDelay="2" AccelFreq="4" Qmax="0" Qmin="-20" />
+ </SimulationObject>
</SimulationObjects>
<Settings>
<Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables</Type>
@@ -8396,8 +8325,8 @@ </FlashSettings>
</SelectedPropertyPackage>
<SimulationMode></SimulationMode>
- <BackupFileName>52647203.dwbcs</BackupFileName>
- <FilePath>C:\Users\prati\OneDrive\Documents\Flowsheet.dwxml</FilePath>
+ <BackupFileName>42126170.dwbcs</BackupFileName>
+ <FilePath>C:\Users\prati\OneDrive\Documents\Flowsheet_backup.dwxml</FilePath>
<FlowsheetQuickConnect>false</FlowsheetQuickConnect>
<FlowsheetShowCalculationQueue>false</FlowsheetShowCalculationQueue>
<FlowsheetShowConsoleWindow>false</FlowsheetShowConsoleWindow>
@@ -8407,7 +8336,7 @@ <FlowsheetSnapToGrid>false</FlowsheetSnapToGrid>
<FlowsheetDisplayGrid>false</FlowsheetDisplayGrid>
<FractionNumberFormat>G8</FractionNumberFormat>
- <Key>66FBB626BBBAA957C066C6EF837D6E27383E68E8</Key>
+ <Key>30E94FC5A32BEA28EDC9EA0E22C39B5B2F9AA6A2</Key>
<NumberFormat>G6</NumberFormat>
<Password></Password>
<SimulationAuthor>PR80\prati</SimulationAuthor>
@@ -8996,8 +8925,8 @@ <Name>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</Name>
<Tag>Make-up</Tag>
<Width>20</Width>
- <X>640.4414</X>
- <Y>256.959</Y>
+ <X>437.419</X>
+ <Y>174.5031</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9043,8 +8972,8 @@ <Name>MAT-db971471-1e8a-42d3-ad06-be461cacea57</Name>
<Tag>Solvent Recovery</Tag>
<Width>20</Width>
- <X>614.9404</X>
- <Y>185.909</Y>
+ <X>411.9181</X>
+ <Y>103.4531</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9090,8 +9019,8 @@ <Name>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name>
<Tag>Feed</Tag>
<Width>20</Width>
- <X>701.6755</X>
- <Y>129.0954</Y>
+ <X>498.6532</X>
+ <Y>46.63944</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9137,8 +9066,8 @@ <Name>MIST-ae80e666-b984-4270-b427-05f406124fe0</Name>
<Tag>MIX-1</Tag>
<Width>20</Width>
- <X>694.7557</X>
- <Y>230.8991</Y>
+ <X>491.7333</X>
+ <Y>148.4432</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9189,8 +9118,8 @@ <Name>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name>
<Tag>S-01</Tag>
<Width>20</Width>
- <X>744.2786</X>
- <Y>241.2887</Y>
+ <X>541.2563</X>
+ <Y>158.8328</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9237,8 +9166,8 @@ <Name>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</Name>
<Tag>EDC-01</Tag>
<Width>144</Width>
- <X>801.1638</X>
- <Y>111.5946</Y>
+ <X>598.1419</X>
+ <Y>29.13858</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9286,8 +9215,8 @@ <Name>MAT-03b2c90d-8474-4909-bef0-39eb7b0a6f41</Name>
<Tag>S-02</Tag>
<Width>20</Width>
- <X>977.8931</X>
- <Y>128.0219</Y>
+ <X>774.8703</X>
+ <Y>45.5659</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9333,8 +9262,8 @@ <Name>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name>
<Tag>Water</Tag>
<Width>20</Width>
- <X>962.1305</X>
- <Y>310.3851</Y>
+ <X>759.1081</X>
+ <Y>227.9292</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9381,8 +9310,8 @@ <Name>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</Name>
<Tag>DC-01</Tag>
<Width>144</Width>
- <X>1044.035</X>
- <Y>127.8646</Y>
+ <X>841.0121</X>
+ <Y>45.40855</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9429,8 +9358,8 @@ <Name>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name>
<Tag>Acetone</Tag>
<Width>20</Width>
- <X>1249.308</X>
- <Y>133.8961</Y>
+ <X>1046.285</X>
+ <Y>51.44016</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9476,8 +9405,8 @@ <Name>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name>
<Tag>3-Methylhexane</Tag>
<Width>20</Width>
- <X>1215.021</X>
- <Y>314.8448</Y>
+ <X>1011.998</X>
+ <Y>232.3888</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9523,8 +9452,8 @@ <Name>RESF-26c14620-b257-493a-b6d0-b997b40f8564</Name>
<Tag>CL-01</Tag>
<Width>25</Width>
- <X>1066.806</X>
- <Y>363.9943</Y>
+ <X>863.7833</X>
+ <Y>281.5383</Y>
<Selected>false</Selected>
<Rotation>180</Rotation>
<DrawMode>2</DrawMode>
@@ -9571,8 +9500,8 @@ <Name>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name>
<Tag>E-01</Tag>
<Width>20</Width>
- <X>1087.98</X>
- <Y>401.1252</Y>
+ <X>884.9571</X>
+ <Y>318.6692</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9618,8 +9547,8 @@ <Name>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name>
<Tag>S-03</Tag>
<Width>20</Width>
- <X>964.8884</X>
- <Y>374.6318</Y>
+ <X>761.8659</X>
+ <Y>292.1758</Y>
<Selected>false</Selected>
<Rotation>181</Rotation>
<DrawMode>2</DrawMode>
@@ -9665,8 +9594,8 @@ <Name>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</Name>
<Tag>R-1</Tag>
<Width>20</Width>
- <X>735.8597</X>
- <Y>347.7545</Y>
+ <X>532.8373</X>
+ <Y>265.2986</Y>
<Selected>false</Selected>
<Rotation>180</Rotation>
<DrawMode>2</DrawMode>
@@ -9685,11 +9614,11 @@ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.MasterTableGraphic</Type>
<ClipboardData>Master Property Table
Object Water Solvent Recovery S-03 S-02 S-01 Make-up Feed Acetone 3-Methylhexane
-Temperature 12.3335 25 25 61.0551 25.0011 25 25 57.7331 95.7602 C
+Temperature 12.3335 25 25 61.0489 25.0013 25 25 57.5626 96.0964 C
Pressure 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 bar
-Mass Flow 20.0582 173.272 173.272 389.252 309.31 150 100 215.979 173.272 kg/h
-Molar Flow 1.06482 2.80861 2.80861 5.61721 4.05372 1.49698 2.62831 2.80861 2.80861 kmol/h
-Volumetric Flow 0.0201646 0.215989 0.215989 0.526433 0.410688 0.219095 0.113715 0.304737 0.231667 m3/h
+Mass Flow 24.8585 163.715 163.715 388.798 313.656 150 100 225.083 163.715 kg/h
+Molar Flow 1.31965 2.80549 2.80549 5.61097 4.30231 1.49698 2.62831 2.80549 2.80549 kmol/h
+Volumetric Flow 0.0249903 0.201037 0.201037 0.525813 0.410532 0.219095 0.113715 0.322089 0.215262 m3/h
Density (Vapor) 0 0 0 0 0 0 0 0 0 kg/m3
Molecular Weight (Vapor) 0 0 0 0 0 0 0 0 0 kg/kmol
Dynamic Viscosity (Vapor) 0 0 0 0 0 0 0 0 0 Pa.s
@@ -9698,19 +9627,19 @@ Compressibility Factor (Vapor) 0 0 0 0 0 0 0 0 0 Molar Fraction (Vapor) 0 0 0 0 0 0 0 0 0
Mass Fraction (Vapor) 0 0 0 0 0 0 0 0 0
Volumetric Fraction (Vapor) 0 0 0 0 0 0 0 0 0
-Density (Liquid 1) 994.725 802.227 802.227 739.414 753.15 684.636 879.388 708.74 747.936 kg/m3
-Molar Weight (Liquid 1) 18.8371 61.6934 61.6934 69.2963 76.3027 100.202 38.0472 76.8992 61.6934 kg/kmol
-Dynamic Viscosity (Liquid 1) 0.00122402 0.000605165 0.000605165 0.000293164 0.000507337 0.000347326 0.000602427 0.00025203 0.000233766 Pa.s
+Density (Liquid 1) 994.725 814.352 814.352 739.421 764.023 684.636 879.388 698.823 760.538 kg/m3
+Molar Weight (Liquid 1) 18.8371 58.3552 58.3552 69.2923 72.9041 100.202 38.0472 80.2295 58.3552 kg/kmol
+Dynamic Viscosity (Liquid 1) 0.00122402 0.000627517 0.000627517 0.000293162 0.000530091 0.000347326 0.000602427 0.000243095 0.000237361 Pa.s
Heat Capacity (Liquid 1) 0 0 0 0 0 0 0 0 0 kJ/[kg.K]
Molar Fraction (Liquid 1) 1 1 1 1 1 1 1 1 1
Mass Fraction (Liquid 1) 1 1 1 1 1 1 1 1 1
Volumetric Fraction (Liquid 1) 1 1 1 1 1 1 1 1 1
-Molar Fraction (Vapor) / Acetone 2.12621E-12 1.07349E-12 1.07349E-12 0.731687 6.69034E-13 0 0.897742 0.754535 4.7154E-13
-Molar Fraction (Liquid 1) / Acetone 9.39876E-15 2.19234E-14 2.19234E-14 0.233952 1.77051E-14 0 0.5 0.467904 2.19234E-14
-Molar Fraction (Vapor) / Water 0.97027 0.253471 0.253471 0.0630818 0.136373 0 0.102258 0.0127444 0.402308
-Molar Fraction (Liquid 1) / Water 0.99 0.46855 0.46855 0.256136 0.290792 0 0.5 0.0437225 0.46855
-Molar Fraction (Vapor) / 3-methylhexane 0.0297297 0.746529 0.746529 0.205231 0.863627 1 0 0.232721 0.597692
-Molar Fraction (Liquid 1) / 3-methylhexane 0.01 0.53145 0.53145 0.509912 0.709208 1 0 0.488374 0.53145
+Molar Fraction (Vapor) / Acetone 2.17409E-12 7.18226E-15 7.18226E-15 0.731778 2.77548E-15 0 0.897742 0.747845 3.06321E-15
+Molar Fraction (Liquid 1) / Acetone 9.61038E-15 1.37309E-16 1.37309E-16 0.234212 6.94179E-17 0 0.5 0.468424 1.37309E-16
+Molar Fraction (Vapor) / Water 0.97027 0.285459 0.285459 0.0630598 0.160744 0 0.102258 0.000854076 0.442586
+Molar Fraction (Liquid 1) / Water 0.99 0.509167 0.509167 0.256051 0.332145 0 0.5 0.00293427 0.509167
+Molar Fraction (Vapor) / 3-methylhexane 0.0297297 0.714541 0.714541 0.205163 0.839256 1 0 0.251301 0.557414
+Molar Fraction (Liquid 1) / 3-methylhexane 0.01 0.490833 0.490833 0.509737 0.667855 1 0 0.528642 0.490833
</ClipboardData>
<NumberOfLines>1</NumberOfLines>
<Padding>4</Padding>
@@ -9761,8 +9690,8 @@ Molar Fraction (Liquid 1) / 3-methylhexane 0.01 0.53145 0.53145 0.509912 0.709 <Name>MASTERTABLE-94b87b53-789f-4e15-9f26-07a3eff3148b</Name>
<Tag></Tag>
<Width>1064</Width>
- <X>457.6452</X>
- <Y>471.6777</Y>
+ <X>254.6228</X>
+ <Y>389.2216</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -11018,7 +10947,7 @@ Molar Fraction (Liquid 1) / 3-methylhexane 0.01 0.53145 0.53145 0.509912 0.709 <PanelLayout><?xml version="1.0" encoding="utf-8"?>
<!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.-->
<!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!-->
-<DockPanel FormatVersion="1.0" DockLeftPortion="562.5" DockRightPortion="0.203007518796992" DockTopPortion="0.25" DockBottomPortion="0.152227705943669" ActiveDocumentPane="0" ActivePane="0">
+<DockPanel FormatVersion="1.0" DockLeftPortion="562.5" DockRightPortion="0.203007518796992" DockTopPortion="0.25" DockBottomPortion="0.152227705943669" ActiveDocumentPane="0" ActivePane="-1">
<Contents Count="10">
<Content ID="0" PersistString="DWSIM.LogPanel" AutoHidePortion="0.152227705943669" IsHidden="True" IsFloat="False" />
<Content ID="1" PersistString="DWSIM.MaterialStreamPanel" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" />
@@ -11503,5 +11432,93 @@ Molar Fraction (Liquid 1) / 3-methylhexane 0.01 0.53145 0.53145 0.509912 0.709 <Message>[11/13/2023 8:34:21 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\ff.pdf.</Message>
<Message>[11/13/2023 8:36:15 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\gg.pdf.</Message>
<Message>[11/13/2023 8:37:14 PM] Flowsheet exported successfully to C:\Users\prati\OneDrive\Documents\gg.pdf.</Message>
+ <Message>[4/13/2024 8:16:39 PM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+ <Message>[4/13/2024 8:16:43 PM] The flowsheet is being calculated, please wait...</Message>
+ <Message>[4/13/2024 8:16:45 PM] EDC-01: Warning!! Estimating activity model parameters</Message>
+ <Message>[4/13/2024 8:16:45 PM] EDC-01: 0 2.5633</Message>
+ <Message>[4/13/2024 8:16:45 PM] EDC-01: 1 2.5691</Message>
+ <Message>[4/13/2024 8:16:45 PM] EDC-01: 2 -0.3165</Message>
+ <Message>[4/13/2024 8:16:45 PM] Warning: EDC-01: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+ <Message>[4/13/2024 8:16:53 PM] DC-01: 0 3.8004</Message>
+ <Message>[4/13/2024 8:16:53 PM] DC-01: 1 3.0538</Message>
+ <Message>[4/13/2024 8:16:53 PM] DC-01: 2 2.1224</Message>
+ <Message>[4/13/2024 8:16:53 PM] DC-01: 3 1.6659</Message>
+ <Message>[4/13/2024 8:16:53 PM] DC-01: 4 1.1256</Message>
+ <Message>[4/13/2024 8:16:54 PM] DC-01: 5 0.6052</Message>
+ <Message>[4/13/2024 8:16:54 PM] DC-01: 6 0.0791</Message>
+ <Message>[4/13/2024 8:16:54 PM] DC-01: 7 -0.4448</Message>
+ <Message>[4/13/2024 8:16:58 PM] The flowsheet was calculated successfully. [15.78s]</Message>
+ <Message>[4/13/2024 8:19:51 PM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+ <Message>[4/13/2024 8:19:52 PM] EDC-01: Warning!! Estimating activity model parameters</Message>
+ <Message>[4/13/2024 8:19:52 PM] EDC-01: 0 2.6698</Message>
+ <Message>[4/13/2024 8:19:52 PM] EDC-01: 1 3.5556</Message>
+ <Message>[4/13/2024 8:19:52 PM] EDC-01: 2 0.6766</Message>
+ <Message>[4/13/2024 8:19:52 PM] EDC-01: 3 -2.8904</Message>
+ <Message>[4/13/2024 8:19:52 PM] Warning: EDC-01: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+ <Message>[4/13/2024 8:19:52 PM] The flowsheet is being calculated, please wait...</Message>
+ <Message>[4/13/2024 8:19:57 PM] DC-01: 0 3.8321</Message>
+ <Message>[4/13/2024 8:19:58 PM] DC-01: 1 3.0455</Message>
+ <Message>[4/13/2024 8:19:58 PM] DC-01: 2 2.0135</Message>
+ <Message>[4/13/2024 8:19:58 PM] DC-01: 3 1.5263</Message>
+ <Message>[4/13/2024 8:19:58 PM] DC-01: 4 0.9591</Message>
+ <Message>[4/13/2024 8:19:58 PM] DC-01: 5 0.4072</Message>
+ <Message>[4/13/2024 8:19:58 PM] DC-01: 6 -0.1488</Message>
+ <Message>[4/13/2024 8:20:02 PM] The flowsheet was calculated successfully. [9.713s]</Message>
+ <Message>[4/13/2024 8:20:40 PM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+ <Message>[4/13/2024 8:20:43 PM] The flowsheet is being calculated, please wait...</Message>
+ <Message>[4/13/2024 8:20:43 PM] EDC-01: Warning!! Estimating activity model parameters</Message>
+ <Message>[4/13/2024 8:20:43 PM] EDC-01: 0 2.6955</Message>
+ <Message>[4/13/2024 8:20:43 PM] EDC-01: 1 1.5990</Message>
+ <Message>[4/13/2024 8:20:43 PM] EDC-01: 2 -1.7852</Message>
+ <Message>[4/13/2024 8:20:43 PM] Warning: EDC-01: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+ <Message>[4/13/2024 8:20:49 PM] DC-01: 0 3.9576</Message>
+ <Message>[4/13/2024 8:20:49 PM] DC-01: 1 3.0498</Message>
+ <Message>[4/13/2024 8:20:49 PM] DC-01: 2 1.8461</Message>
+ <Message>[4/13/2024 8:20:49 PM] DC-01: 3 1.1452</Message>
+ <Message>[4/13/2024 8:20:49 PM] DC-01: 4 0.4180</Message>
+ <Message>[4/13/2024 8:20:49 PM] DC-01: 5 -0.3143</Message>
+ <Message>[4/13/2024 8:20:53 PM] The flowsheet was calculated successfully. [9.825s]</Message>
+ <Message>[4/13/2024 8:21:16 PM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+ <Message>[4/13/2024 8:21:21 PM] EDC-01: Warning!! Estimating activity model parameters</Message>
+ <Message>[4/13/2024 8:21:21 PM] EDC-01: 0 2.6866</Message>
+ <Message>[4/13/2024 8:21:21 PM] EDC-01: 1 0.2889</Message>
+ <Message>[4/13/2024 8:21:21 PM] EDC-01: 2 -3.0551</Message>
+ <Message>[4/13/2024 8:21:21 PM] Warning: EDC-01: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+ <Message>[4/13/2024 8:21:22 PM] The flowsheet is being calculated, please wait...</Message>
+ <Message>[4/13/2024 8:21:27 PM] DC-01: 0 4.0561</Message>
+ <Message>[4/13/2024 8:21:27 PM] DC-01: 1 3.0133</Message>
+ <Message>[4/13/2024 8:21:27 PM] DC-01: 2 1.9059</Message>
+ <Message>[4/13/2024 8:21:27 PM] DC-01: 3 1.0865</Message>
+ <Message>[4/13/2024 8:21:28 PM] DC-01: 4 0.2493</Message>
+ <Message>[4/13/2024 8:21:28 PM] DC-01: 5 -0.5969</Message>
+ <Message>[4/13/2024 8:21:32 PM] The flowsheet was calculated successfully. [10.19s]</Message>
+ <Message>[4/13/2024 8:22:49 PM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+ <Message>[4/13/2024 8:22:51 PM] EDC-01: Warning!! Estimating activity model parameters</Message>
+ <Message>[4/13/2024 8:22:51 PM] EDC-01: 0 2.7168</Message>
+ <Message>[4/13/2024 8:22:51 PM] EDC-01: 1 -0.6743</Message>
+ <Message>[4/13/2024 8:22:51 PM] Warning: EDC-01: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+ <Message>[4/13/2024 8:22:51 PM] The flowsheet is being calculated, please wait...</Message>
+ <Message>[4/13/2024 8:22:56 PM] DC-01: 0 3.8978</Message>
+ <Message>[4/13/2024 8:22:56 PM] DC-01: 1 3.0344</Message>
+ <Message>[4/13/2024 8:22:56 PM] DC-01: 2 1.7369</Message>
+ <Message>[4/13/2024 8:22:56 PM] DC-01: 3 1.1535</Message>
+ <Message>[4/13/2024 8:22:57 PM] DC-01: 4 0.5168</Message>
+ <Message>[4/13/2024 8:22:57 PM] DC-01: 5 -0.1122</Message>
+ <Message>[4/13/2024 8:23:00 PM] The flowsheet was calculated successfully. [9.975s]</Message>
+ <Message>[4/13/2024 8:23:53 PM] Caught unhandled exception: Object reference not set to an instance of an object.</Message>
+ <Message>[4/13/2024 8:23:56 PM] EDC-01: Warning!! Estimating activity model parameters</Message>
+ <Message>[4/13/2024 8:23:56 PM] EDC-01: 0 2.6779</Message>
+ <Message>[4/13/2024 8:23:56 PM] EDC-01: 1 -0.5693</Message>
+ <Message>[4/13/2024 8:23:56 PM] Warning: EDC-01: PVF flash of bottom product failed: Temperature deviation too large; reflashing using TP flash</Message>
+ <Message>[4/13/2024 8:23:56 PM] The flowsheet is being calculated, please wait...</Message>
+ <Message>[4/13/2024 8:24:01 PM] DC-01: 0 3.7925</Message>
+ <Message>[4/13/2024 8:24:01 PM] DC-01: 1 3.0934</Message>
+ <Message>[4/13/2024 8:24:01 PM] DC-01: 2 2.0897</Message>
+ <Message>[4/13/2024 8:24:01 PM] DC-01: 3 1.6560</Message>
+ <Message>[4/13/2024 8:24:01 PM] DC-01: 4 1.1271</Message>
+ <Message>[4/13/2024 8:24:02 PM] DC-01: 5 0.6178</Message>
+ <Message>[4/13/2024 8:24:02 PM] DC-01: 6 0.1021</Message>
+ <Message>[4/13/2024 8:24:02 PM] DC-01: 7 -0.4114</Message>
+ <Message>[4/13/2024 8:24:05 PM] The flowsheet was calculated successfully. [9.919s]</Message>
</MessagesLog>
</DWSIM_Simulation_Data>
\ No newline at end of file diff --git a/Simulation_Of_Wastewater_Treatment_Plant-Degradation_Of_Malathion_By_Ms_Atshaya_T/user_defined_compound/Alum.json b/Simulation_Of_Wastewater_Treatment_Plant-Degradation_Of_Malathion_By_Ms_Atshaya_T/user_defined_compound/Alum.json new file mode 100644 index 0000000..51a7771 --- /dev/null +++ b/Simulation_Of_Wastewater_Treatment_Plant-Degradation_Of_Malathion_By_Ms_Atshaya_T/user_defined_compound/Alum.json @@ -0,0 +1,199 @@ +{
+ "Acentric_Factor": 0.0,
+ "BO_BSW": 0.0,
+ "BO_GOR": 0.0,
+ "BO_OilVisc1": 0.0,
+ "BO_OilVisc2": 0.0,
+ "BO_OilViscTemp1": 0.0,
+ "BO_OilViscTemp2": 0.0,
+ "BO_PNA_A": 0.0,
+ "BO_PNA_N": 0.0,
+ "BO_PNA_P": 0.0,
+ "BO_SGG": 0.0,
+ "BO_SGO": 0.0,
+ "CAS_Number": "10043-01-3",
+ "Chao_Seader_Acentricity": 0.0,
+ "Chao_Seader_Liquid_Molar_Volume": 0.0,
+ "Chao_Seader_Solubility_Parameter": 0.0,
+ "Charge": 0,
+ "ChemicalStructure": "",
+ "Comments": "",
+ "CompCreatorStudyFile": "",
+ "COSMODBName": null,
+ "Critical_Compressibility": 0.0,
+ "Critical_Pressure": 0.0,
+ "Critical_Temperature": 0.0,
+ "Critical_Volume": 0.0,
+ "CurrentDB": "User",
+ "Dipole_Moment": 0.0,
+ "Electrolyte_Cp0": 0.0,
+ "Electrolyte_DelGF": 0.0,
+ "Electrolyte_DelHF": 0.0,
+ "EnthalpyOfFusionAtTf": 0.0,
+ "Formula": "A12(SO4)3",
+ "HVap_A": 0.0,
+ "HVap_B": 0.0,
+ "HVap_C": 0.0,
+ "HVap_D": 0.0,
+ "HVap_E": 0.0,
+ "HVap_TMAX": 0.0,
+ "HVap_TMIN": 0.0,
+ "HydrationNumber": 0.0,
+ "ID": 734708,
+ "Ideal_Gas_Heat_Capacity_Const_A": 0.0,
+ "Ideal_Gas_Heat_Capacity_Const_B": 0.0,
+ "Ideal_Gas_Heat_Capacity_Const_C": 0.0,
+ "Ideal_Gas_Heat_Capacity_Const_D": 0.0,
+ "Ideal_Gas_Heat_Capacity_Const_E": 0.0,
+ "IdealgasCpEquation": "",
+ "IG_Enthalpy_of_Formation_25C": 0.0,
+ "IG_Entropy_of_Formation_25C": 0.0,
+ "IG_Gibbs_Energy_of_Formation_25C": 0.0,
+ "InChI": "",
+ "Ion_CpAq_a": 0.0,
+ "Ion_CpAq_b": 0.0,
+ "Ion_CpAq_c": 0.0,
+ "IsBlackOil": false,
+ "IsCOOLPROPSupported": false,
+ "IsFPROPSSupported": false,
+ "IsHydratedSalt": false,
+ "IsHYPO": 0,
+ "IsIon": false,
+ "IsModified": false,
+ "IsPF": 0,
+ "IsSalt": false,
+ "Liquid_Density_Const_A": 0.0,
+ "Liquid_Density_Const_B": 0.0,
+ "Liquid_Density_Const_C": 0.0,
+ "Liquid_Density_Const_D": 0.0,
+ "Liquid_Density_Const_E": 0.0,
+ "Liquid_Density_Tmax": 0.0,
+ "Liquid_Density_Tmin": 0.0,
+ "Liquid_Heat_Capacity_Const_A": 0.0,
+ "Liquid_Heat_Capacity_Const_B": 0.0,
+ "Liquid_Heat_Capacity_Const_C": 0.0,
+ "Liquid_Heat_Capacity_Const_D": 0.0,
+ "Liquid_Heat_Capacity_Const_E": 0.0,
+ "Liquid_Heat_Capacity_Tmax": 0.0,
+ "Liquid_Heat_Capacity_Tmin": 0.0,
+ "Liquid_Thermal_Conductivity_Const_A": 0.0,
+ "Liquid_Thermal_Conductivity_Const_B": 0.0,
+ "Liquid_Thermal_Conductivity_Const_C": 0.0,
+ "Liquid_Thermal_Conductivity_Const_D": 0.0,
+ "Liquid_Thermal_Conductivity_Const_E": 0.0,
+ "Liquid_Thermal_Conductivity_Tmax": 0.0,
+ "Liquid_Thermal_Conductivity_Tmin": 0.0,
+ "Liquid_Viscosity_Const_A": 0.0,
+ "Liquid_Viscosity_Const_B": 0.0,
+ "Liquid_Viscosity_Const_C": 0.0,
+ "Liquid_Viscosity_Const_D": 0.0,
+ "Liquid_Viscosity_Const_E": 0.0,
+ "LiquidDensityEquation": "",
+ "LiquidHeatCapacityEquation": "",
+ "LiquidThermalConductivityEquation": "",
+ "LiquidViscosityEquation": "",
+ "Molar_Weight": 0.0,
+ "MolarVolume_k1i": 0.0,
+ "MolarVolume_k2i": 0.0,
+ "MolarVolume_k3i": 0.0,
+ "MolarVolume_v2i": 0.0,
+ "MolarVolume_v3i": 0.0,
+ "Name": "Aluminium Sulfate",
+ "NBP": null,
+ "NegativeIon": "",
+ "NegativeIonStoichCoeff": 0,
+ "Normal_Boiling_Point": 0.0,
+ "OriginalDB": "User",
+ "PC_SAFT_epsilon_k": 0.0,
+ "PC_SAFT_m": 0.0,
+ "PC_SAFT_sigma": 0.0,
+ "PF_MM": null,
+ "PF_SG": null,
+ "PF_Tv1": null,
+ "PF_Tv2": null,
+ "PF_v1": null,
+ "PF_v2": null,
+ "PF_vA": null,
+ "PF_vB": null,
+ "PF_Watson_K": null,
+ "PositiveIon": "",
+ "PositiveIonStoichCoeff": 0,
+ "PR_Volume_Translation_Coefficient": 0.0,
+ "SMILES": "",
+ "Solid_Density_Const_A": 0.0,
+ "Solid_Density_Const_B": 0.0,
+ "Solid_Density_Const_C": 0.0,
+ "Solid_Density_Const_D": 0.0,
+ "Solid_Density_Const_E": 0.0,
+ "Solid_Density_Tmax": 0.0,
+ "Solid_Density_Tmin": 0.0,
+ "Solid_Heat_Capacity_Const_A": 0.0,
+ "Solid_Heat_Capacity_Const_B": 0.0,
+ "Solid_Heat_Capacity_Const_C": 0.0,
+ "Solid_Heat_Capacity_Const_D": 0.0,
+ "Solid_Heat_Capacity_Const_E": 0.0,
+ "Solid_Heat_Capacity_Tmax": 0.0,
+ "Solid_Heat_Capacity_Tmin": 0.0,
+ "SolidDensityAtTs": 0.0,
+ "SolidDensityEquation": "",
+ "SolidHeatCapacityEquation": "",
+ "SolidTs": 0.0,
+ "SRK_Volume_Translation_Coefficient": 0.0,
+ "StandardStateMolarVolume": 0.0,
+ "StoichSum": 0,
+ "Surface_Tension_Const_A": 0.0,
+ "Surface_Tension_Const_B": 0.0,
+ "Surface_Tension_Const_C": 0.0,
+ "Surface_Tension_Const_D": 0.0,
+ "Surface_Tension_Const_E": 0.0,
+ "Surface_Tension_Tmax": 0.0,
+ "Surface_Tension_Tmin": 0.0,
+ "SurfaceTensionEquation": "",
+ "TemperatureOfFusion": 0.0,
+ "UNIQUAC_Q": 0.0,
+ "UNIQUAC_R": 0.0,
+ "Vapor_Pressure_Constant_A": 0.0,
+ "Vapor_Pressure_Constant_B": 0.0,
+ "Vapor_Pressure_Constant_C": 0.0,
+ "Vapor_Pressure_Constant_D": 0.0,
+ "Vapor_Pressure_Constant_E": 0.0,
+ "Vapor_Pressure_TMAX": 0.0,
+ "Vapor_Pressure_TMIN": 0.0,
+ "Vapor_Thermal_Conductivity_Const_A": 0.0,
+ "Vapor_Thermal_Conductivity_Const_B": 0.0,
+ "Vapor_Thermal_Conductivity_Const_C": 0.0,
+ "Vapor_Thermal_Conductivity_Const_D": 0.0,
+ "Vapor_Thermal_Conductivity_Const_E": 0.0,
+ "Vapor_Thermal_Conductivity_Tmax": 0.0,
+ "Vapor_Thermal_Conductivity_Tmin": 0.0,
+ "Vapor_Viscosity_Const_A": 0.0,
+ "Vapor_Viscosity_Const_B": 0.0,
+ "Vapor_Viscosity_Const_C": 0.0,
+ "Vapor_Viscosity_Const_D": 0.0,
+ "Vapor_Viscosity_Const_E": 0.0,
+ "Vapor_Viscosity_Tmax": 0.0,
+ "Vapor_Viscosity_Tmin": 0.0,
+ "VaporizationEnthalpyEquation": "",
+ "VaporPressureEquation": "",
+ "VaporThermalConductivityEquation": "",
+ "VaporViscosityEquation": "",
+ "Z_Rackett": 0.0,
+ "Elements": {
+ "A": 12.0,
+ "O": 12.0,
+ "S": 3.0
+ },
+ "MODFACGroups": {},
+ "NISTMODFACGroups": {},
+ "UNIFACGroups": {},
+ "FullerDiffusionVolume": 0.0,
+ "LennardJonesDiameter": 0.0,
+ "LennardJonesEnergy": 0.0,
+ "Parachor": 0.0,
+ "Tag": "",
+ "ExtraProperties": {},
+ "COSTALD_SRK_Acentric_Factor": 0.0,
+ "COSTALD_Characteristic_Volume": 0.0,
+ "IsSolid": false,
+ "ChemSepFamily": 1000
+}
\ No newline at end of file |