From 7203193da4f00033fc19deb81f263e2b35966ac6 Mon Sep 17 00:00:00 2001
From: Sashi20
Date: Mon, 16 Jun 2025 00:20:16 +0550
Subject: 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

---
 .../user_defined_compound/143191sodiumoleate.json  |  338 +
 .../Abstract.pdf                                   |  Bin 238630 -> 0 bytes
 .../Flowsheet.dwxml                                | 9016 --------------------
 .../ABSTRACT.pdf                                   |  Bin 0 -> 324242 bytes
 .../Abstract.pdf                                   |  Bin 196914 -> 0 bytes
 .../Flowsheet.dwxmz                                |  Bin 168525 -> 168772 bytes
 6 files changed, 338 insertions(+), 9016 deletions(-)
 create mode 100644 Design_And_Simulation_Of_Natural_Soap_Production_Via_Saponification_Using_Dwsim_By_Mr_Shiv_Pratap_Gupta/user_defined_compound/143191sodiumoleate.json
 delete mode 100644 Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf
 delete mode 100644 Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Flowsheet.dwxml
 create mode 100644 Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/ABSTRACT.pdf
 delete mode 100644 Tnt_Production_By_Nitration_Of_Toluene_By_Mr_Dhruv_Thakare/Abstract.pdf

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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+}
\ 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
Binary files a/Heterogeneous_Catalyst_Design_For_Efficient_Isobutane_Dehydrogenation_To_Isobutene_By_Mr_Sai_Sidharth_A/Abstract.pdf and /dev/null 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
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-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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-              <DynamicProperties />
-            </Compound>
-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Liquid1</ComponentName>
-          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
-          <Name>Liquid1</Name>
-          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
-            <surfaceTension>NaN</surfaceTension>
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-            <idealGasHeatCapacityCp>1.69530338075069</idealGasHeatCapacityCp>
-            <idealGasHeatCapacityRatio>1.09215173759631</idealGasHeatCapacityRatio>
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-        <Phase>
-          <ID>4</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
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-              <DynamicProperties />
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-            <Compound>
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-              <DynamicProperties />
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-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Liquid2</ComponentName>
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-        <Phase>
-          <ID>5</ID>
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-            <Compound>
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-              <ComponentDescription></ComponentDescription>
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-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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-        <Phase>
-          <ID>6</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Isobutane</ComponentName>
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-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Aqueous</ComponentName>
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-        <Phase>
-          <ID>7</ID>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <ComponentName>Isobutane</ComponentName>
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-              <FugacityCoeff>NaN</FugacityCoeff>
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-              <DynamicProperties />
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-            <Compound>
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-      <UserDefinedChartNames />
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-          <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
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-          <PropertyType>System.String</PropertyType>
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-        <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>
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-        <SortableItem>Molar Fraction (Mixture) / Isobutene | DESC</SortableItem>
-        <SortableItem>Molar Fraction (Mixture) / Hydrogen | ASC</SortableItem>
-        <SortableItem>Molar Fraction (Mixture) / Hydrogen | DESC</SortableItem>
-        <SortableItem>Custom</SortableItem>
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-      <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>
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-      <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
-      <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
-      <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
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-      <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>
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-      <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
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-      <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
-      <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
-      <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
-      <DisplayMissingCompoundPropertiesWarning>false</DisplayMissingCompoundPropertiesWarning>
-      <ForcedSolids>[]</ForcedSolids>
-      <PropertyOverrides>{}</PropertyOverrides>
-      <InteractionParameters />
-      <FlashSettings>
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-        <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>
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-      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
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-      <BO_OilViscTemp2>0</BO_OilViscTemp2>
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-      <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>
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-      <Name>Isobutene</Name>
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-  <MessagesLog>
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-    <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>
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-    <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
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-- 
cgit