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authorSashi202025-06-16 00:20:16 +0550
committerSashi202025-06-16 00:20:16 +0550
commit7203193da4f00033fc19deb81f263e2b35966ac6 (patch)
tree32fa8aa54f4e325da099d1e85bb9e7f8d8fb963c
parenta14933c7919226db98fefd7b68b695ff2d9848cb (diff)
downloadDWSIM-Flowsheets-7203193da4f00033fc19deb81f263e2b35966ac6.tar.gz
DWSIM-Flowsheets-7203193da4f00033fc19deb81f263e2b35966ac6.tar.bz2
DWSIM-Flowsheets-7203193da4f00033fc19deb81f263e2b35966ac6.zip
Added(A)/Deleted(D) following Flowsheet file
A Design_And_Simulation_Of_Natural_Soap_Production_Via_Saponification_Using_Dwsim_By_Mr_Shiv_Pratap_Gupta/user_defined_compound/143191sodiumoleate.json D Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf D Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml A Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/ABSTRACT.pdf D Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Abstract.pdf M Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Flowsheet.dwxmz
-rw-r--r--Design_And_Simulation_Of_Natural_Soap_Production_Via_Saponification_Using_Dwsim_By_Mr_Shiv_Pratap_Gupta/user_defined_compound/143191sodiumoleate.json338
-rw-r--r--Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdfbin238630 -> 0 bytes
-rw-r--r--Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml9016
-rw-r--r--Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/ABSTRACT.pdfbin0 -> 324242 bytes
-rw-r--r--Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Abstract.pdfbin196914 -> 0 bytes
-rw-r--r--Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Flowsheet.dwxmzbin168525 -> 168772 bytes
6 files changed, 338 insertions, 9016 deletions
diff --git a/Design_And_Simulation_Of_Natural_Soap_Production_Via_Saponification_Using_Dwsim_By_Mr_Shiv_Pratap_Gupta/user_defined_compound/143191sodiumoleate.json b/Design_And_Simulation_Of_Natural_Soap_Production_Via_Saponification_Using_Dwsim_By_Mr_Shiv_Pratap_Gupta/user_defined_compound/143191sodiumoleate.json
new file mode 100644
index 0000000..de6ad87
--- /dev/null
+++ b/Design_And_Simulation_Of_Natural_Soap_Production_Via_Saponification_Using_Dwsim_By_Mr_Shiv_Pratap_Gupta/user_defined_compound/143191sodiumoleate.json
@@ -0,0 +1,338 @@
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+ "IG_Gibbs_Energy_of_Formation_25C": -577.091918376595,
+ "InChI": "",
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+ "SurfaceTensionEquation": "",
+ "TemperatureOfFusion": 448.14,
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+ "Vapor_Viscosity_Tmax": 0.0,
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+ "VaporizationEnthalpyEquation": "",
+ "VaporPressureEquation": "",
+ "VaporThermalConductivityEquation": "",
+ "VaporViscosityEquation": "",
+ "Z_Rackett": 0.16979224954680056,
+ "Elements": {
+ "C": 18.0,
+ "H": 33.0,
+ "Na": 1.0,
+ "O": 2.0
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+ "MODFACGroups": {},
+ "NISTMODFACGroups": {},
+ "UNIFACGroups": {
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+ "6": 1
+ },
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+ "Tag": "",
+ "ExtraProperties": {},
+ "COSTALD_SRK_Acentric_Factor": 0.0,
+ "COSTALD_Characteristic_Volume": 0.0,
+ "IsSolid": false,
+ "ChemSepFamily": 1000,
+ "Vapor_Pressure_Regression_Fit": 0.0,
+ "Vapor_Pressure_Tabular_Data": {
+ "XName": "",
+ "YName": "",
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+ },
+ "Ideal_Gas_Heat_Capacity_Regression_Fit": 0.0,
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+ "Liquid_Viscosity_Regression_Fit": 0.0,
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+ "YUnit": "",
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+ "Source": "",
+ "Comments": ""
+ },
+ "Liquid_Density_Regression_Fit": 0.0,
+ "Liquid_Density_Tabular_Data": {
+ "XName": "",
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+ "Liquid_Heat_Capacity_Regression_Fit": 0.0,
+ "Liquid_Heat_Capacity_Tabular_Data": {
+ "XName": "",
+ "YName": "",
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+ },
+ "Liquid_Thermal_Conductivity_Regression_Fit": 0.0,
+ "Liquid_Thermal_Conductivity_Tabular_Data": {
+ "XName": "",
+ "YName": "",
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+ "XData": [],
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+ },
+ "Vapor_Thermal_Conductivity_Regression_Fit": 0.0,
+ "Vapor_Thermal_Conductivity_Tabular_Data": {
+ "XName": "",
+ "YName": "",
+ "XUnit": "",
+ "YUnit": "",
+ "XData": [],
+ "YData": [],
+ "Source": "",
+ "Comments": ""
+ },
+ "Vapor_Viscosity_Regression_Fit": 0.0,
+ "Vapor_Viscosity_Tabular_Data": {
+ "XName": "",
+ "YName": "",
+ "XUnit": "",
+ "YUnit": "",
+ "XData": [],
+ "YData": [],
+ "Source": "",
+ "Comments": ""
+ },
+ "Solid_Density_Regression_Fit": 0.0,
+ "Solid_Density_Tabular_Data": {
+ "XName": "",
+ "YName": "",
+ "XUnit": "",
+ "YUnit": "",
+ "XData": [],
+ "YData": [],
+ "Source": "",
+ "Comments": ""
+ },
+ "Surface_Tension_Regression_Fit": 0.0,
+ "Surface_Tension_Tabular_Data": {
+ "XName": "",
+ "YName": "",
+ "XUnit": "",
+ "YUnit": "",
+ "XData": [],
+ "YData": [],
+ "Source": "",
+ "Comments": ""
+ },
+ "Solid_Heat_Capacity_Regression_Fit": 0.0,
+ "Solid_Heat_Capacity_Tabular_Data": {
+ "XName": "",
+ "YName": "",
+ "XUnit": "",
+ "YUnit": "",
+ "XData": [],
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+ "Source": "",
+ "Comments": ""
+ },
+ "Enthalpy_Of_Vaporization_Regression_Fit": 0.0,
+ "Enthalpy_Of_Vaporization_Tabular_Data": {
+ "XName": "",
+ "YName": "",
+ "XUnit": "",
+ "YUnit": "",
+ "XData": [],
+ "YData": [],
+ "Source": "",
+ "Comments": ""
+ },
+ "StandardHeatOfCombustion_LHV": 0.0
+} \ No newline at end of file
diff --git a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf b/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf
deleted file mode 100644
index f162bbf..0000000
--- a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf
+++ /dev/null
Binary files differ
diff --git a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml b/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml
deleted file mode 100644
index ecd62fd..0000000
--- a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml
+++ /dev/null
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- <PartialVolume>8.88395976096247E-05</PartialVolume>
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- <Compound>
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- <PartialVolume>8.15793244523351E-05</PartialVolume>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
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- <Compound>
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- <PartialVolume>2.55002235074774E-05</PartialVolume>
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- </Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>OverallLiquid</ComponentName>
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
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- <Compound>
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Vapor</ComponentName>
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- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid3</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid3</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>6</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Isobutane</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Isobutane</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Isobutene</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Isobutene</Name>
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- <PartialVolume>0</PartialVolume>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
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- <PetroleumFraction>false</PetroleumFraction>
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- <Kvalue>0</Kvalue>
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- <Name>Hydrogen</Name>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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- <DynamicProperties />
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
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- <Properties>
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- <PropertyType>System.String</PropertyType>
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- <Property>
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- <PropertyType>System.String</PropertyType>
- <Data>"Empties the volume content on the next run."</Data>
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- <DynamicPropertiesUnitTypes>
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- <Molarity>0</Molarity>
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- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>NaN</MassFlow>
- <MolarFlow>NaN</MolarFlow>
- <Name>Isobutene</Name>
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- <PartialVolume>0.000113772032683781</PartialVolume>
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- <DiffusionCoefficient>0</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Hydrogen</ComponentName>
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- <Molality>0</Molality>
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- <MolarFlow>NaN</MolarFlow>
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- <PartialVolume>2.55002235074774E-05</PartialVolume>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
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- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>OverallLiquid</ComponentName>
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- <Properties>
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- <kinematic_viscosity>0</kinematic_viscosity>
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- <massfraction>0</massfraction>
- <molar_enthalpy>NaN</molar_enthalpy>
- <molar_entropy>NaN</molar_entropy>
- <molarflow>0</molarflow>
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- <molecularWeight>NaN</molecularWeight>
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- <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
- <molar_internal_energy>NaN</molar_internal_energy>
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- <Compound>
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- <Name>Isobutene</Name>
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Vapor</ComponentName>
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- <molar_entropyF>-1.80494161718591</molar_entropyF>
- <molarflow>34.7214969009902</molarflow>
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- <volumetric_flow>0.434837196514017</volumetric_flow>
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- <idealGasHeatCapacityRatio>1.40065055494714</idealGasHeatCapacityRatio>
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- <Compound>
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- <ComponentDescription></ComponentDescription>
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- <Compound>
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- <NumberFormat>G6</NumberFormat>
- <Password></Password>
- <SimulationAuthor>SAISIDHARTH_NB\aruls</SimulationAuthor>
- <SimulationComments></SimulationComments>
- <SimulationName>MySimulation_35</SimulationName>
- <UsePassword>false</UsePassword>
- <SelectedUnitSystem1>
- <Type>DWSIM.SharedClasses.SystemsOfUnits.SI_ENG</Type>
- <accel>m2/s</accel>
- <activity>Pa</activity>
- <activityCoefficient>-</activityCoefficient>
- <area>m2</area>
- <cakeresistance>m/kg</cakeresistance>
- <cinematic_viscosity>cSt</cinematic_viscosity>
- <compressibility>1/Pa</compressibility>
- <compressibilityfactor>-</compressibilityfactor>
- <deltaP>bar</deltaP>
- <deltaT>C.</deltaT>
- <density>kg/m3</density>
- <diameter>mm</diameter>
- <distance>m</distance>
- <enthalpy>kJ/kg</enthalpy>
- <entropy>kJ/[kg.K]</entropy>
- <excessEnthalpy>kJ/kg</excessEnthalpy>
- <excessEntropy>kJ/[kg.K]</excessEntropy>
- <force>N</force>
- <foulingfactor>K.m2/W</foulingfactor>
- <fugacity>Pa</fugacity>
- <fugacityCoefficient>-</fugacityCoefficient>
- <gor>m3/m3</gor>
- <head>m</head>
- <heat_transf_coeff>W/[m2.K]</heat_transf_coeff>
- <heatCapacityCp>kJ/[kg.K]</heatCapacityCp>
- <heatCapacityCv>kJ/[kg.K]</heatCapacityCv>
- <heatflow>kW</heatflow>
- <heat>kJ</heat>
- <idealGasHeatCapacity>kJ/[kg.K]</idealGasHeatCapacity>
- <jouleThomsonCoefficient>K/Pa</jouleThomsonCoefficient>
- <kvalue>-</kvalue>
- <logfugacityCoefficient>-</logfugacityCoefficient>
- <logKvalue>-</logKvalue>
- <mass>kg</mass>
- <mass_conc>kg/m3</mass_conc>
- <massflow>kg/h</massflow>
- <massfraction>-</massfraction>
- <mediumresistance>m-1</mediumresistance>
- <molar_conc>mol/m3</molar_conc>
- <molar_enthalpy>kJ/kmol</molar_enthalpy>
- <molar_entropy>kJ/[kmol.K]</molar_entropy>
- <molar_volume>m3/kmol</molar_volume>
- <molarflow>kmol/h</molarflow>
- <molarfraction>-</molarfraction>
- <molecularWeight>kg/kmol</molecularWeight>
- <Name>SI (Engineering)</Name>
- <pdp_boilingPointTemperature>C</pdp_boilingPointTemperature>
- <pdp_meltingTemperature>C</pdp_meltingTemperature>
- <pressure>bar</pressure>
- <reac_rate>mol/[m3.s]</reac_rate>
- <reac_rate_heterog>mol/[kg.s]</reac_rate_heterog>
- <spec_vol>m3/kg</spec_vol>
- <speedOfSound>m/s</speedOfSound>
- <surfaceTension>N/m</surfaceTension>
- <temperature>C</temperature>
- <thermalConductivity>W/[m.K]</thermalConductivity>
- <thermalConductivityOfLiquid>W/[m.K]</thermalConductivityOfLiquid>
- <thermalConductivityOfVapor>W/[m.K]</thermalConductivityOfVapor>
- <thickness>mm</thickness>
- <time>s</time>
- <vaporPressure>bar</vaporPressure>
- <velocity>m/s</velocity>
- <viscosity>cP</viscosity>
- <viscosityOfLiquid>cP</viscosityOfLiquid>
- <viscosityOfVapor>cP</viscosityOfVapor>
- <volume>m3</volume>
- <volumetricFlow>m3/h</volumetricFlow>
- <diffusivity>m2/s</diffusivity>
- <conductance>[kg/s]/[Pa^0.5]</conductance>
- <mole>kmol</mole>
- <emission_factor>[kg/s]/kW</emission_factor>
- <specific_power>kW/[ton/h]</specific_power>
- </SelectedUnitSystem1>
- <SimultaneousAdjustSolverEnabled>true</SimultaneousAdjustSolverEnabled>
- <SpreadsheetUseRegionalSeparator>false</SpreadsheetUseRegionalSeparator>
- <EnergyBalanceCheck>ShowWarning</EnergyBalanceCheck>
- <MassBalanceCheck>ShowWarning</MassBalanceCheck>
- <EnergyBalanceRelativeTolerance>0.01</EnergyBalanceRelativeTolerance>
- <MassBalanceRelativeTolerance>0.01</MassBalanceRelativeTolerance>
- <DisplayCornerPropertyList>false</DisplayCornerPropertyList>
- <DisplayCornerPropertyListPosition>RightBottom</DisplayCornerPropertyListPosition>
- <DisplayFloatingPropertyTables>true</DisplayFloatingPropertyTables>
- <DisplayCornerPropertyListFontColor>DimGray</DisplayCornerPropertyListFontColor>
- <DisplayCornerPropertyListFontName>Consolas</DisplayCornerPropertyListFontName>
- <DisplayCornerPropertyListFontSize>8</DisplayCornerPropertyListFontSize>
- <DisplayCornerPropertyListPadding>4</DisplayCornerPropertyListPadding>
- <DefaultFloatingTableCompoundAmountBasis>Molar_Fractions</DefaultFloatingTableCompoundAmountBasis>
- <DisplayFloatingTableCompoundAmounts>true</DisplayFloatingTableCompoundAmounts>
- <SpreadsheetUnitLockingMode>true</SpreadsheetUnitLockingMode>
- <CompoundOrderingMode>AsAdded</CompoundOrderingMode>
- <FlowsheetControlPanelMode>false</FlowsheetControlPanelMode>
- <SkipEquilibriumCalculationOnDefinedStreams>true</SkipEquilibriumCalculationOnDefinedStreams>
- <ForceStreamPhase>None</ForceStreamPhase>
- <DisplayUserDefinedPropertiesEditor>false</DisplayUserDefinedPropertiesEditor>
- <LabelFontSize>10</LabelFontSize>
- <FlowsheetColorTheme>0</FlowsheetColorTheme>
- <RegularFontName>OpenSans_SemiCondensed-Regular</RegularFontName>
- <BoldFontName>OpenSans_SemiCondensed-SemiBold</BoldFontName>
- <ItalicFontName>OpenSans_SemiCondensed-Italic</ItalicFontName>
- <BoldItalicFontName>OpenSans_SemiCondensed-MediumItalic</BoldItalicFontName>
- <DisplayEnergyStreamPowerValue>true</DisplayEnergyStreamPowerValue>
- <DisplayMaterialStreamMassFlowValue>false</DisplayMaterialStreamMassFlowValue>
- <DisplayMaterialStreamMolarFlowValue>false</DisplayMaterialStreamMolarFlowValue>
- <DisplayMaterialStreamVolFlowValue>false</DisplayMaterialStreamVolFlowValue>
- <DisplayMaterialStreamTemperatureValue>false</DisplayMaterialStreamTemperatureValue>
- <DisplayMaterialStreamPressureValue>false</DisplayMaterialStreamPressureValue>
- <DisplayMaterialStreamEnergyFlowValue>false</DisplayMaterialStreamEnergyFlowValue>
- <AddObjectsWithStreams>2</AddObjectsWithStreams>
- <DisplayDynamicPropertyValues>true</DisplayDynamicPropertyValues>
- <CurrentWeather>
- <Type>DWSIM.SharedClasses.WeatherData</Type>
- <CurrentCondition>Sunny</CurrentCondition>
- <WindSpeed_km_h>5</WindSpeed_km_h>
- <RelativeHumidity_pct>30</RelativeHumidity_pct>
- <Temperature_C>30</Temperature_C>
- <SolarIrradiation_kWh_m2>1</SolarIrradiation_kWh_m2>
- <Latitude>0</Latitude>
- <Longitude>0</Longitude>
- <AtmosphericPressure_Pa>101325</AtmosphericPressure_Pa>
- </CurrentWeather>
- <CustomCalculationOrder />
- <SpecCalculationMode>AfterSourceObject</SpecCalculationMode>
- <ForceObjectSolving>true</ForceObjectSolving>
- <SaveFlowsheetMessagesInFile>true</SaveFlowsheetMessagesInFile>
- <RTFAnnotations></RTFAnnotations>
- <EnabledUndoRedo>true</EnabledUndoRedo>
- <EnableGHGEmissionsSubsystem>false</EnableGHGEmissionsSubsystem>
- <FlowsheetTransitionObject>
- <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetTransitionRestore</Type>
- <FeatureName></FeatureName>
- <FeatureType></FeatureType>
- <Action></Action>
- <Location></Location>
- <Position />
- </FlowsheetTransitionObject>
- <UniqueID>c101119b-444f-4de0-8d83-b13c6f989585</UniqueID>
- <VisibleProperties>
- <ObjectType Value="AbsorptionColumn">
- <PropertyID Value="PROP_AC_0" />
- <PropertyID Value="PROP_AC_1" />
- <PropertyID Value="PROP_AC_2" />
- <PropertyID Value="Estimated Height" />
- <PropertyID Value="Estimated Diameter" />
- <PropertyID Value="Number of Stages" />
- </ObjectType>
- <ObjectType Value="Adjust">
- <PropertyID Value="MinVal" />
- <PropertyID Value="MaxVal" />
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- <PropertyID Value="Tolerance" />
- <PropertyID Value="StepSize" />
- <PropertyID Value="MaximumIterations" />
- </ObjectType>
- <ObjectType Value="AnalogGauge">
- <PropertyID Value="Monitored Value" />
- </ObjectType>
- <ObjectType Value="CapeOpenUO" />
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- <PropertyID Value="PROP_CP_0" />
- <PropertyID Value="SpecifiedStreamIndex" />
- </ObjectType>
- <ObjectType Value="Compressor">
- <PropertyID Value="PROP_CO_0" />
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- <PropertyID Value="PROP_CO_3" />
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- <PropertyID Value="PolytropicEfficiency" />
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- <PropertyID Value="PolytropicCoefficient" />
- <PropertyID Value="AdiabaticHead" />
- <PropertyID Value="PolytropicHead" />
- <PropertyID Value="RotationSpeed" />
- <PropertyID Value="PressureRatio" />
- </ObjectType>
- <ObjectType Value="Cooler">
- <PropertyID Value="PROP_CL_0" />
- <PropertyID Value="PROP_CL_1" />
- <PropertyID Value="PROP_CL_2" />
- <PropertyID Value="PROP_CL_3" />
- <PropertyID Value="PROP_CL_4" />
- <PropertyID Value="PROP_CL_5" />
- </ObjectType>
- <ObjectType Value="CustomUO" />
- <ObjectType Value="DigitalGauge">
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- </ObjectType>
- <ObjectType Value="DistillationColumn">
- <PropertyID Value="PROP_DC_2" />
- <PropertyID Value="PROP_DC_5" />
- <PropertyID Value="PROP_DC_6" />
- <PropertyID Value="PROP_DC_7" />
- <PropertyID Value="PROP_DC_8" />
- <PropertyID Value="Condenser_Specification_Value" />
- <PropertyID Value="Reboiler_Specification_Value" />
- <PropertyID Value="Global_Stage_Efficiency" />
- <PropertyID Value="Condenser_Calculated_Value" />
- <PropertyID Value="Reboiler_Calculated_Value" />
- <PropertyID Value="Estimated Height" />
- <PropertyID Value="Estimated Diameter" />
- </ObjectType>
- <ObjectType Value="DummyUnitOperation" />
- <ObjectType Value="EnergyRecycle">
- <PropertyID Value="PROP_ER_0" />
- <PropertyID Value="PROP_ER_1" />
- <PropertyID Value="PROP_ER_2" />
- </ObjectType>
- <ObjectType Value="EnergyStream">
- <PropertyID Value="PROP_ES_0" />
- </ObjectType>
- <ObjectType Value="ExcelUO">
- <PropertyID Value="Calc_dQ" />
- </ObjectType>
- <ObjectType Value="Expander">
- <PropertyID Value="PROP_TU_0" />
- <PropertyID Value="PROP_TU_1" />
- <PropertyID Value="PROP_TU_2" />
- <PropertyID Value="PROP_TU_3" />
- <PropertyID Value="PROP_TU_4" />
- <PropertyID Value="PolytropicEfficiency" />
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- <PropertyID Value="PolytropicCoefficient" />
- <PropertyID Value="AdiabaticHead" />
- <PropertyID Value="PolytropicHead" />
- <PropertyID Value="RotationSpeed" />
- <PropertyID Value="PressureRatio" />
- </ObjectType>
- <ObjectType Value="Filter">
- <PropertyID Value="PROP_FT_0" />
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- <PropertyID Value="PROP_FT_3" />
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- </ObjectType>
- <ObjectType Value="Flowsheet" />
- <ObjectType Value="Heater">
- <PropertyID Value="PROP_HT_0" />
- <PropertyID Value="PROP_HT_1" />
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- <PropertyID Value="PROP_HT_3" />
- <PropertyID Value="PROP_HT_4" />
- <PropertyID Value="PROP_HT_5" />
- </ObjectType>
- <ObjectType Value="HeatExchanger">
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- </ObjectType>
- <ObjectType Value="Input" />
- <ObjectType Value="LevelGauge">
- <PropertyID Value="Monitored Value" />
- </ObjectType>
- <ObjectType Value="MaterialStream">
- <PropertyID Value="PROP_MS_0" />
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- <PropertyID Value="PROP_MS_2" />
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- <PropertyID Value="PROP_MS_4" />
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- <PropertyID Value="PROP_MS_10" />
- <PropertyID Value="PROP_MS_27" />
- <PropertyID Value="PROP_MS_130" />
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- <ObjectType Value="Mixer" />
- <ObjectType Value="OrificePlate">
- <PropertyID Value="PROP_OP_0" />
- <PropertyID Value="PROP_OP_1" />
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- <PropertyID Value="PROP_OP_3" />
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- <ObjectType Value="PIDController">
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- <PropertyID Value="LastError" />
- <PropertyID Value="CurrentError" />
- <PropertyID Value="CumulativeError" />
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- <ObjectType Value="Pipe">
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- <PropertyID Value="PROP_PS_2" />
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- <PropertyID Value="PROP_PS_9" />
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- <ObjectType Value="Pump">
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- <ObjectType Value="PythonController">
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- <ObjectType Value="Reactor_Equilibrium">
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- <PropertyID Value="Calculation Mode" />
- <PropertyID Value="Initial Gibbs Energy" />
- <PropertyID Value="Final Gibbs Energy" />
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- <ObjectType Value="Reactor_Gibbs">
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- <PropertyID Value="Final Gibbs Energy" />
- <PropertyID Value="Element Balance Residue" />
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- <ObjectType Value="Reactor_PFR">
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- <ObjectType Value="Recycle">
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- <PropertyID Value="Actual Flow Coefficient" />
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- <ObjectType Value="Vessel">
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- <ObjectType Value="NeuralNetworkUnitOperation">
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- <ObjectType Value="PipeNetworkUnitOperation">
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- <PropertyID Value="Energy Balance Residual" />
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- <ObjectType Value="HydroelectricTurbine">
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- <PropertyID Value="Maximum Theoretical Power" />
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- <Description>Material Stream Heater</Description>
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- <PROP_MS_260>false</PROP_MS_260>
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- </Properties>
- <SortableItems>
- <SortableItem>Name | ASC</SortableItem>
- <SortableItem>Name | DESC</SortableItem>
- <SortableItem>Temperature | ASC</SortableItem>
- <SortableItem>Temperature | DESC</SortableItem>
- <SortableItem>Pressure | ASC</SortableItem>
- <SortableItem>Pressure | DESC</SortableItem>
- <SortableItem>Mass Flow | ASC</SortableItem>
- <SortableItem>Mass Flow | DESC</SortableItem>
- <SortableItem>Molar Flow | ASC</SortableItem>
- <SortableItem>Molar Flow | DESC</SortableItem>
- <SortableItem>Molar Fraction (Mixture) / Isobutane | ASC</SortableItem>
- <SortableItem>Molar Fraction (Mixture) / Isobutane | DESC</SortableItem>
- <SortableItem>Molar Fraction (Mixture) / Isobutene | ASC</SortableItem>
- <SortableItem>Molar Fraction (Mixture) / Isobutene | DESC</SortableItem>
- <SortableItem>Molar Fraction (Mixture) / Hydrogen | ASC</SortableItem>
- <SortableItem>Molar Fraction (Mixture) / Hydrogen | DESC</SortableItem>
- <SortableItem>Custom</SortableItem>
- </SortableItems>
- </GraphicObject>
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- <PropertyPackages>
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- <ID>PP-cb481779-6616-4ab7-b966-bf6af4f09801</ID>
- <Type>DWSIM.Thermodynamics.PropertyPackages.PengRobinsonPropertyPackage</Type>
- <ComponentName>Peng-Robinson (PR)</ComponentName>
- <ComponentDescription>Property Package that uses the Peng-Robinson Cubic Equation of State. Recommended for use with hydrocarbons and non-condensables.</ComponentDescription>
- <Tag>Peng-Robinson (PR) (1)</Tag>
- <UseHenryConstants>true</UseHenryConstants>
- <AutoEstimateMissingNRTLUNIQUACParameters>true</AutoEstimateMissingNRTLUNIQUACParameters>
- <SingleCompoundCheckThreshold>0.99999</SingleCompoundCheckThreshold>
- <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
- <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
- <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
- <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
- <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
- <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
- <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
- <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
- <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
- <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
- <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
- <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
- <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
- <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
- <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
- <EnthalpyEntropyCpCvCalculationMode>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
- <LiquidEnthalpyEntropyCpCvCalculationMode_EOS>EOS</LiquidEnthalpyEntropyCpCvCalculationMode_EOS>
- <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
- <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
- <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
- <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
- <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
- <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
- <DisplayMissingCompoundPropertiesWarning>false</DisplayMissingCompoundPropertiesWarning>
- <ForcedSolids>[]</ForcedSolids>
- <PropertyOverrides>{}</PropertyOverrides>
- <InteractionParameters />
- <FlashSettings>
- <Setting Name="Replace_PTFlash" Value="False" />
- <Setting Name="ValidateEquilibriumCalc" Value="False" />
- <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
- <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
- <Setting Name="ValidationGibbsTolerance" Value="0.01" />
- <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
- <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
- <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
- <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
- <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
- <Setting Name="NL_FastMode" Value="True" />
- <Setting Name="IO_FastMode" Value="True" />
- <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
- <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
- <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
- <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
- <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
- <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
- <Setting Name="ST_Number_of_Random_Tries" Value="20" />
- <Setting Name="CheckIncipientLiquidForStability" Value="False" />
- <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
- <Setting Name="PTFlash_DampingFactor" Value="1.0" />
- <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
- <Setting Name="ImmiscibleWaterOption" Value="False" />
- <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
- <Setting Name="UseIOFlash" Value="False" />
- <Setting Name="GibbsMinimizationExternalSolver" Value="" />
- <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
- <Setting Name="PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases" Value="False" />
- <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
- <Setting Name="FailSafeCalculationMode" Value="1" />
- </FlashSettings>
- </PropertyPackage>
- </PropertyPackages>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
- <Acentric_Factor>0.186</Acentric_Factor>
- <BO_BSW>0</BO_BSW>
- <BO_GOR>0</BO_GOR>
- <BO_OilVisc1>0</BO_OilVisc1>
- <BO_OilVisc2>0</BO_OilVisc2>
- <BO_OilViscTemp1>0</BO_OilViscTemp1>
- <BO_OilViscTemp2>0</BO_OilViscTemp2>
- <BO_PNA_A>0</BO_PNA_A>
- <BO_PNA_N>0</BO_PNA_N>
- <BO_PNA_P>0</BO_PNA_P>
- <BO_SGG>0</BO_SGG>
- <BO_SGO>0</BO_SGO>
- <CAS_Number>75-28-5</CAS_Number>
- <Chao_Seader_Acentricity>0.1825</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>105.5</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0.00328800419366</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
- <CompCreatorStudyFile></CompCreatorStudyFile>
- <Critical_Compressibility>0.278</Critical_Compressibility>
- <Critical_Pressure>3640000</Critical_Pressure>
- <Critical_Temperature>407.85</Critical_Temperature>
- <Critical_Volume>0.2627</Critical_Volume>
- <CurrentDB>ChemSep</CurrentDB>
- <Dipole_Moment>4.4E-31</Dipole_Moment>
- <Electrolyte_Cp0>0</Electrolyte_Cp0>
- <Electrolyte_DelGF>0</Electrolyte_DelGF>
- <Electrolyte_DelHF>0</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>4.54</EnthalpyOfFusionAtTf>
- <Formula>CH3CH(CH3)CH3</Formula>
- <HVap_A>34869000</HVap_A>
- <HVap_B>0.64449</HVap_B>
- <HVap_C>-0.15424</HVap_C>
- <HVap_D>-0.28822</HVap_D>
- <HVap_E>0.20982</HVap_E>
- <HVap_TMAX>407.8</HVap_TMAX>
- <HVap_TMIN>113.54</HVap_TMIN>
- <HydrationNumber>0</HydrationNumber>
- <ID>4</ID>
- <Ideal_Gas_Heat_Capacity_Const_A>39746.03</Ideal_Gas_Heat_Capacity_Const_A>
- <Ideal_Gas_Heat_Capacity_Const_B>-371.573</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>12.02593</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>0.000755039</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>-2.59608E-07</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>16</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-2322.52048270712</IG_Enthalpy_of_Formation_25C>
- <IG_Entropy_of_Formation_25C>-6.55254904594069</IG_Entropy_of_Formation_25C>
- <IG_Gibbs_Energy_of_Formation_25C>-368.877984659906</IG_Gibbs_Energy_of_Formation_25C>
- <InChI></InChI>
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- <Ion_CpAq_c>0</Ion_CpAq_c>
- <IsBlackOil>false</IsBlackOil>
- <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
- <IsFPROPSSupported>false</IsFPROPSSupported>
- <IsHydratedSalt>false</IsHydratedSalt>
- <IsHYPO>0</IsHYPO>
- <IsIon>false</IsIon>
- <IsModified>false</IsModified>
- <IsPF>0</IsPF>
- <IsSalt>false</IsSalt>
- <Liquid_Density_Const_A>0.89934</Liquid_Density_Const_A>
- <Liquid_Density_Const_B>0.25371</Liquid_Density_Const_B>
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- <Liquid_Density_Const_D>0.25125</Liquid_Density_Const_D>
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- <Liquid_Heat_Capacity_Const_A>89466</Liquid_Heat_Capacity_Const_A>
- <Liquid_Heat_Capacity_Const_B>-323.61</Liquid_Heat_Capacity_Const_B>
- <Liquid_Heat_Capacity_Const_C>12.827</Liquid_Heat_Capacity_Const_C>
- <Liquid_Heat_Capacity_Const_D>-0.010476</Liquid_Heat_Capacity_Const_D>
- <Liquid_Heat_Capacity_Const_E>2.5037E-05</Liquid_Heat_Capacity_Const_E>
- <Liquid_Heat_Capacity_Tmax>380</Liquid_Heat_Capacity_Tmax>
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- <Liquid_Thermal_Conductivity_Const_E>-1.7826E-05</Liquid_Thermal_Conductivity_Const_E>
- <Liquid_Thermal_Conductivity_Tmax>400</Liquid_Thermal_Conductivity_Tmax>
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- <Liquid_Viscosity_Const_A>-39.10125</Liquid_Viscosity_Const_A>
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- <Molar_Weight>58.1222</Molar_Weight>
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- <Enthalpy_Of_Vaporization_Regression_Fit>0</Enthalpy_Of_Vaporization_Regression_Fit>
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- <StandardHeatOfCombustion_LHV>-119957.537154989</StandardHeatOfCombustion_LHV>
- <DynamicProperties />
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- <MODFACGroups />
- <NISTMODFACGroups />
- <Elements>
- <Item Name="H" Value="2" />
- </Elements>
- </Compound>
- </Compounds>
- <ReactionSets>
- <ReactionSet>
- <ID>DefaultSet</ID>
- <Name>Default Set</Name>
- <Description>Default Reaction Set</Description>
- <Reactions>
- <Reaction Key="ff2db60c-ff59-401a-8ee5-c6a658130587" ReactionID="ff2db60c-ff59-401a-8ee5-c6a658130587" Rank="0" IsActive="true" />
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- <Description></Description>
- <Equation>CH3CH(CH3)CH3 &lt;--&gt; CH2C(CH3)2 + H2 </Equation>
- <ID>ff2db60c-ff59-401a-8ee5-c6a658130587</ID>
- <Name>rxn1</Name>
- <ReactionBasis>PartialPress</ReactionBasis>
- <ReactionHeat>117890</ReactionHeat>
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- <ReactionPhase>Vapor</ReactionPhase>
- <ReactionType>Heterogeneous_Catalytic</ReactionType>
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- <KExprType>Gibbs</KExprType>
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- <Rate>0</Rate>
- <RateEquationDenominator>1 + (6.34E-2 * exp(-31.59 / (8.314 * (T + 273.15))) * R1) + (2.41E-4 * exp(-64.78 / (8.314 * (T + 273.15))) * P1) + (8.20E-5 * exp(-57.90 / (8.314 * (T + 273.15))) * P2)</RateEquationDenominator>
- <RateEquationNumerator>(1.67E+6 * exp(-101.31 / (8.314 * (T + 273.15)))) * R1</RateEquationNumerator>
- <ReactionGibbsEnergy>79520.0000000002</ReactionGibbsEnergy>
- <Tmax>2000</Tmax>
- <Tmin>0</Tmin>
- <VelUnit>kmol/[kg.s]</VelUnit>
- <ReactionKinFwdType>Arrhenius</ReactionKinFwdType>
- <ReactionKinRevType>Arrhenius</ReactionKinRevType>
- <ReactionKinFwdExpression></ReactionKinFwdExpression>
- <ReactionKinRevExpression></ReactionKinRevExpression>
- <E_Forward_Unit>J/mol</E_Forward_Unit>
- <E_Reverse_Unit>J/mol</E_Reverse_Unit>
- <ReactionKinetics>Expression</ReactionKinetics>
- <ScriptTitle></ScriptTitle>
- <EquilibriumReactionBasisUnits>Pa</EquilibriumReactionBasisUnits>
- <Compounds>
- <Compound Name="Isobutane" StoichCoeff="-1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="true" />
- <Compound Name="Isobutene" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
- <Compound Name="Hydrogen" StoichCoeff="1" DirectOrder="0" ReverseOrder="0" IsBaseReactant="false" />
- </Compounds>
- </Reaction>
- </Reactions>
- <StoredSolutions />
- <DynamicsManager>
- <Type>DWSIM.DynamicsManager.Manager</Type>
- <Description></Description>
- <CurrentSchedule></CurrentSchedule>
- <ScheduleList />
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- </DynamicsManager>
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- <OptimizationCase>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.OptimizationCase</Type>
- <name>optcase0</name>
- <description></description>
- <stats></stats>
- <solvm>AL_BRENT</solvm>
- <maxits>100</maxits>
- <tolerance>1E-06</tolerance>
- <epsX>0.001</epsX>
- <epsF>0.001</epsF>
- <epsG>0.001</epsG>
- <epsilon>0.001</epsilon>
- <barriermultiplier>0.0001</barriermultiplier>
- <numdevscheme>2</numdevscheme>
- <boundvariables>false</boundvariables>
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- <Variables />
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- <SensitivityAnalysis>
- <SensitivityAnalysisCase>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SensitivityAnalysisCase</Type>
- <iv1>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
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- <Variables />
- <DepVariables />
- </SensitivityAnalysisCase>
- </SensitivityAnalysis>
- <PetroleumAssays />
- <WatchItems />
- <ScriptItems />
- <ChartItems />
- <ParticleSizeDistributions />
- <Spreadsheet>
- <RGFData>{"MAIN":"{\"?xml\":{\"@version\":\"1.0\"},\"grid\":{\"@xmlns:xsd\":\"http://www.w3.org/2001/XMLSchema\",\"@xmlns:xsi\":\"http://www.w3.org/2001/XMLSchema-instance\",\"head\":{\"meta\":{\"culture\":\"en-US\",\"editor\":\"ReoGrid Core\",\"core-ver\":\"2.1.0.0\"},\"rows\":\"65536\",\"cols\":\"100\",\"default-row-height\":\"20\",\"default-col-width\":\"70\",\"focus-forward-direction\":\"down\",\"settings\":{\"@meta\":\"30475026398\"},\"script\":null},\"style\":{\"@font\":\"Arial\",\"@font-size\":\"10\",\"@align\":\"general\",\"@valign\":\"middle\"},\"rows\":null,\"cols\":null,\"v-borders\":null,\"h-borders\":null,\"cells\":null}}"}</RGFData>
- </Spreadsheet>
- <PanelLayout>&lt;?xml version="1.0" encoding="utf-8"?&gt;
-&lt;!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.--&gt;
-&lt;!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!--&gt;
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- &lt;Contents Count="12"&gt;
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- &lt;DockWindow ID="3" DockState="DockTop" ZOrderIndex="5"&gt;
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- <MessagesLog>
- <Message>[2/15/2025 10:05:28 AM] The flowsheet was calculated successfully. [0.393s]</Message>
- <Message>[2/15/2025 10:05:39 AM] The flowsheet was calculated successfully. [0.005565s]</Message>
- <Message>[2/15/2025 10:05:42 AM] The flowsheet was calculated successfully. [0.02188s]</Message>
- <Message>[2/15/2025 10:06:01 AM] 2: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:01 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:01 AM] The flowsheet was calculated successfully. [0.005778s]</Message>
- <Message>[2/15/2025 10:06:03 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:03 AM] The flowsheet was calculated successfully. [0.01177s]</Message>
- <Message>[2/15/2025 10:06:18 AM] The flowsheet was calculated successfully. [0.003548s]</Message>
- <Message>[2/15/2025 10:06:23 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:23 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:23 AM] The flowsheet was calculated successfully. [0.01476s]</Message>
- <Message>[2/15/2025 10:06:28 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:28 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:28 AM] The flowsheet was calculated successfully. [0.003794s]</Message>
- <Message>[2/15/2025 10:06:31 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:31 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:31 AM] The flowsheet was calculated successfully. [0.004002s]</Message>
- <Message>[2/15/2025 10:06:33 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:33 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:33 AM] The flowsheet was calculated successfully. [0.004006s]</Message>
- <Message>[2/15/2025 10:06:41 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:41 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:41 AM] The flowsheet was calculated successfully. [0.01041s]</Message>
- <Message>[2/15/2025 10:06:44 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:44 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:06:44 AM] The flowsheet was calculated successfully. [0.003186s]</Message>
- <Message>[2/15/2025 10:08:08 AM] 4: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:08:08 AM] 6: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:08:08 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:08:08 AM] 8: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:08:08 AM] The flowsheet was calculated successfully. [4.191s]</Message>
- <Message>[2/15/2025 10:08:54 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:08:54 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:08:55 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:08:55 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:09:04 AM] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[2/15/2025 10:09:04 AM] Error in 'CS-1': Calculated negative molar flow for stream 8, compound Hydrogen [-7.105427357601E-15 mol/s]. (ComponentSeparator.vb, 199)</Message>
- <Message>[2/15/2025 10:09:25 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:09:25 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:09:26 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:09:26 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:09:27 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:09:27 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:09:31 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:09:31 AM] The flowsheet was calculated successfully. [8.54s]</Message>
- <Message>[2/15/2025 10:09:42 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:09:42 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:09:42 AM] The calculator is busy, please wait...</Message>
- <Message>[2/15/2025 10:09:42 AM] Dynamic Mode is currently enabled.</Message>
- <Message>[2/15/2025 10:09:48 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:09:48 AM] The flowsheet was calculated successfully. [8.447s]</Message>
- <Message>[2/15/2025 10:10:13 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:10:13 AM] The flowsheet was calculated successfully. [8.466s]</Message>
- <Message>[2/15/2025 10:10:43 AM] 7: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[2/15/2025 10:10:43 AM] The flowsheet was calculated successfully. [8.464s]</Message>
- <Message>[3/8/2025 9:06:13 AM] File C:\Users\aruls\OneDrive\Desktop\Recent_works\flowsheeting\Flowsheet.dwxml saved successfully.</Message>
- <Message>[3/8/2025 10:35:58 AM] S-02: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[3/8/2025 10:35:59 AM] S-05: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[3/8/2025 10:35:59 AM] The flowsheet was calculated successfully. [9.024s]</Message>
- <Message>[3/8/2025 5:25:34 PM] S-02: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[3/8/2025 5:25:34 PM] S-05: Single-compound Stream detected. Switching to PH Flash</Message>
- <Message>[3/8/2025 5:25:34 PM] The flowsheet was calculated successfully. [8.971s]</Message>
- </MessagesLog>
- <Results>
- <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetResults</Type>
- <TotalCAPEX>0</TotalCAPEX>
- <TotalOPEX>0</TotalOPEX>
- <ResidualMassBalance>-5.81246162312254E-12</ResidualMassBalance>
- <TotalEnergyBalance>-5032.08577856815</TotalEnergyBalance>
- <AdditionalResults />
- </Results>
- <GHGCompositions />
-</DWSIM_Simulation_Data> \ No newline at end of file
diff --git a/Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/ABSTRACT.pdf b/Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/ABSTRACT.pdf
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diff --git a/Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Flowsheet.dwxmz b/Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Flowsheet.dwxmz
index 99e296a..206d9cc 100644
--- a/Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Flowsheet.dwxmz
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