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authorSashi202021-03-01 00:20:14 +0550
committerSashi202021-03-01 00:20:14 +0550
commitb722974b7a19a3ab53a059ad44e673b176514266 (patch)
tree2b37bd8eab4b3864db5c0b2ad4ba00a10c02fbaf
parent35f83e90be50f3bd52dcdf2aedbf9c6829d7ca21 (diff)
downloadDWSIM-Flowsheets-b722974b7a19a3ab53a059ad44e673b176514266.tar.gz
DWSIM-Flowsheets-b722974b7a19a3ab53a059ad44e673b176514266.tar.bz2
DWSIM-Flowsheets-b722974b7a19a3ab53a059ad44e673b176514266.zip
Added(A)/Deleted(D) following Flowsheet file
A Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/Decomposition_of_MTBE_in_a_Reactive_distillation_column.pdf A Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/MTBE_decomposition.dwxmz A Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/ExtractiveDistillationforHeptane.pdf A Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/heptanetolueneextractionfinal.dwxmz A Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdf A Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmz A Production_Of_Ethanol_By_Fermentation_Of_Glucose_By_Ms_Yutika_Naik/user_defined_compound/glucose.zip A Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/Formaldehyde_Production.dwxmz A Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdf
-rw-r--r--Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/Decomposition_of_MTBE_in_a_Reactive_distillation_column.pdfbin0 -> 466702 bytes
-rw-r--r--Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/MTBE_decomposition.dwxmzbin0 -> 50507 bytes
-rw-r--r--Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/ExtractiveDistillationforHeptane.pdfbin0 -> 162523 bytes
-rw-r--r--Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/heptanetolueneextractionfinal.dwxmzbin0 -> 77193 bytes
-rw-r--r--Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdfbin0 -> 330765 bytes
-rw-r--r--Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmzbin0 -> 64530 bytes
-rw-r--r--Production_Of_Ethanol_By_Fermentation_Of_Glucose_By_Ms_Yutika_Naik/user_defined_compound/glucose.zip195
-rw-r--r--Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/Formaldehyde_Production.dwxmzbin0 -> 89066 bytes
-rw-r--r--Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdfbin0 -> 409063 bytes
9 files changed, 195 insertions, 0 deletions
diff --git a/Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/Decomposition_of_MTBE_in_a_Reactive_distillation_column.pdf b/Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/Decomposition_of_MTBE_in_a_Reactive_distillation_column.pdf
new file mode 100644
index 0000000..8098145
--- /dev/null
+++ b/Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/Decomposition_of_MTBE_in_a_Reactive_distillation_column.pdf
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diff --git a/Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/MTBE_decomposition.dwxmz b/Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/MTBE_decomposition.dwxmz
new file mode 100644
index 0000000..df6ce2b
--- /dev/null
+++ b/Decomposition_Of_Mtbe_In_A_Reactive_Distillation_Column_By_Ms_Patel_Bharvi/MTBE_decomposition.dwxmz
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diff --git a/Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/ExtractiveDistillationforHeptane.pdf b/Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/ExtractiveDistillationforHeptane.pdf
new file mode 100644
index 0000000..a876eb8
--- /dev/null
+++ b/Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/ExtractiveDistillationforHeptane.pdf
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diff --git a/Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/heptanetolueneextractionfinal.dwxmz b/Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/heptanetolueneextractionfinal.dwxmz
new file mode 100644
index 0000000..80aea89
--- /dev/null
+++ b/Extractive_Distillation_For_Heptane-Toluene_Separation_By_Ms_Yutika_Naik/heptanetolueneextractionfinal.dwxmz
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diff --git a/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdf b/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdf
new file mode 100644
index 0000000..feab026
--- /dev/null
+++ b/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdf
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diff --git a/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmz b/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmz
new file mode 100644
index 0000000..a16b4db
--- /dev/null
+++ b/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmz
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diff --git a/Production_Of_Ethanol_By_Fermentation_Of_Glucose_By_Ms_Yutika_Naik/user_defined_compound/glucose.zip b/Production_Of_Ethanol_By_Fermentation_Of_Glucose_By_Ms_Yutika_Naik/user_defined_compound/glucose.zip
new file mode 100644
index 0000000..8f52c18
--- /dev/null
+++ b/Production_Of_Ethanol_By_Fermentation_Of_Glucose_By_Ms_Yutika_Naik/user_defined_compound/glucose.zip
@@ -0,0 +1,195 @@
+{
+ "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": "4205-23-6",
+ "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": 6631370.0,
+ "Critical_Temperature": 1034.02,
+ "Critical_Volume": 0.46,
+ "CurrentDB": "User",
+ "Dipole_Moment": 0.0,
+ "Electrolyte_Cp0": 0.0,
+ "Electrolyte_DelGF": 0.0,
+ "Electrolyte_DelHF": 0.0,
+ "EnthalpyOfFusionAtTf": 0.0,
+ "Formula": "C6H12O6",
+ "HVap_A": 957.55265705015563,
+ "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": 31360,
+ "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": "0",
+ "IG_Enthalpy_of_Formation_25C": -5745.004440497336,
+ "IG_Entropy_of_Formation_25C": 0.0,
+ "IG_Gibbs_Energy_of_Formation_25C": -4405.7504440497332,
+ "InChI": "1S/C6H12O6/c7-1-3(9)5(11)6(12)4(10)2-8/h1,3-6,8-12H,2H2/t3-,4+,5-,6-/m1/s1",
+ "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": "0",
+ "LiquidHeatCapacityEquation": "0",
+ "LiquidThermalConductivityEquation": "0",
+ "LiquidViscosityEquation": "0",
+ "Molar_Weight": 180.16,
+ "MolarVolume_k1i": 0.0,
+ "MolarVolume_k2i": 0.0,
+ "MolarVolume_k3i": 0.0,
+ "MolarVolume_v2i": 0.0,
+ "MolarVolume_v3i": 0.0,
+ "Name": "glucose",
+ "NBP": 844.48,
+ "NegativeIon": "",
+ "NegativeIonStoichCoeff": 0,
+ "Normal_Boiling_Point": 844.48,
+ "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,
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+ "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": "O=CC(O)C(O)C(O)C(O)CO",
+ "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": "0",
+ "SolidHeatCapacityEquation": "0",
+ "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": 443.48,
+ "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": "0",
+ "VaporThermalConductivityEquation": "",
+ "VaporViscosityEquation": "",
+ "Z_Rackett": 0.0,
+ "Elements": {
+ "C": 6.0,
+ "H": 12.0,
+ "O": 6.0
+ },
+ "MODFACGroups": {},
+ "NISTMODFACGroups": {},
+ "UNIFACGroups": {},
+ "FullerDiffusionVolume": 0.0,
+ "LennardJonesDiameter": 0.0,
+ "LennardJonesEnergy": 0.0,
+ "Parachor": 0.0,
+ "Tag": "",
+ "ExtraProperties": {}
+} \ No newline at end of file
diff --git a/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/Formaldehyde_Production.dwxmz b/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/Formaldehyde_Production.dwxmz
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diff --git a/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdf b/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdf
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index 0000000..41b65c6
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+++ b/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdf
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