7 files changed, 205 insertions, 0 deletions
diff --git a/Heterogeneous_Azeotropic_Distillation_Conventional_Had_For_Dehydration_Of_Tert_Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/ABSTRACT.pdf b/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/ABSTRACT.pdf
index 3c55576..3c55576 100644
--- a/Heterogeneous_Azeotropic_Distillation_Conventional_Had_For_Dehydration_Of_Tert_Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/ABSTRACT.pdf
+++ b/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/ABSTRACT.pdf
diff --git a/Heterogeneous_Azeotropic_Distillation_Conventional_Had_For_Dehydration_Of_Tert_Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/Flowsheet.dwxmz b/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/Flowsheet.dwxmz
index 9dc1d52..9dc1d52 100644
--- a/Heterogeneous_Azeotropic_Distillation_Conventional_Had_For_Dehydration_Of_Tert_Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/Flowsheet.dwxmz
+++ b/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/Flowsheet.dwxmz
diff --git a/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/README.txt b/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/README.txt
new file mode 100644
index 0000000..60f8ccf
--- /dev/null
+++ b/Conventional_Heterogeneous_Azeotropic_Distillation_For_Dehydration_Of_Tert-Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Conventional Heterogeneous Azeotropic Distillation for Dehydration of tert-Butanol
+Proposar Name: Mr Richard Carlos Rojas Quintero
+University: Escuela Superior Politécnica De Chimborazo, Ecuador
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Improvement_Of_The_Monochlorobenzene_Separation_Process_Through_Heat_Integration_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt b/Improvement_Of_The_Monochlorobenzene_Separation_Process_Through_Heat_Integration_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt
new file mode 100644
index 0000000..31814e4
--- /dev/null
+++ b/Improvement_Of_The_Monochlorobenzene_Separation_Process_Through_Heat_Integration_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Improvement of the MonoChlorobenzene Separation Process through Heat Integration
+Proposar Name: Ms Ana Paula Ribeiro Paiva
+University: Universidade Federal Fluminense, Rio de Janeiro
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Phthalic_Anhydride_Production_Process_By_Mr_Prakash_M/user_defined_compound/Phthalicanhydride.json b/Phthalic_Anhydride_Production_Process_By_Mr_Prakash_M/user_defined_compound/Phthalicanhydride.json
new file mode 100644
index 0000000..648559f
--- /dev/null
+++ b/Phthalic_Anhydride_Production_Process_By_Mr_Prakash_M/user_defined_compound/Phthalicanhydride.json
@@ -0,0 +1,189 @@
+{
+  "Acentric_Factor": 0.12315081089492874,
+  "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": "85-44-9",
+  "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": 0.048571368343963812,
+  "Critical_Pressure": 7831466.8337379582,
+  "Critical_Temperature": 339.38356164383561,
+  "Critical_Volume": 0.0175,
+  "CurrentDB": "User",
+  "Dipole_Moment": 0.0,
+  "Electrolyte_Cp0": 0.0,
+  "Electrolyte_DelGF": 0.0,
+  "Electrolyte_DelHF": 0.0,
+  "EnthalpyOfFusionAtTf": -0.88,
+  "Formula": "C8H4O3",
+  "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": 738773,
+  "Ideal_Gas_Heat_Capacity_Const_A": -37930.0,
+  "Ideal_Gas_Heat_Capacity_Const_B": 210.0,
+  "Ideal_Gas_Heat_Capacity_Const_C": -0.391,
+  "Ideal_Gas_Heat_Capacity_Const_D": 0.000206,
+  "Ideal_Gas_Heat_Capacity_Const_E": 0.0,
+  "IdealgasCpEquation": "4",
+  "IG_Enthalpy_of_Formation_25C": "Infinity",
+  "IG_Entropy_of_Formation_25C": 0.0,
+  "IG_Gibbs_Energy_of_Formation_25C": "Infinity",
+  "InChI": "1S/C8H4O3/c9-7-5-3-1-2-4-6(5)8(10)11-7/h1-4H",
+  "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": "Phthalic Anhydride",
+  "NBP": 557.2,
+  "NegativeIon": "",
+  "NegativeIonStoichCoeff": 0,
+  "Normal_Boiling_Point": 198.2,
+  "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": "O=C1OC(=O)c2ccccc21",
+  "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": 122.5,
+  "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": 0.048571368343963812,
+  "Elements": {},
+  "MODFACGroups": {},
+  "NISTMODFACGroups": {},
+  "UNIFACGroups": {},
+  "FullerDiffusionVolume": 0.0,
+  "LennardJonesDiameter": 0.0,
+  "LennardJonesEnergy": 0.0,
+  "Parachor": 0.0
+}
+\ No newline at end of file
diff --git a/Power_Cycle_Based_On_Cold_Energy_Of_Liquefied_Natural_Gas_And_Low-Grade_Heat_Source_By_Mrs_Deepthi_Chittalury/Abstract.pdf b/Power_Cycle_Based_On_Cold_Energy_Of_Lng_And_Low-Grade_Heat_Source_By_Ms_Deepthi_Chittalury/Abstract.pdf
index 6e4824c..6e4824c 100644
--- a/Power_Cycle_Based_On_Cold_Energy_Of_Liquefied_Natural_Gas_And_Low-Grade_Heat_Source_By_Mrs_Deepthi_Chittalury/Abstract.pdf
+++ b/Power_Cycle_Based_On_Cold_Energy_Of_Lng_And_Low-Grade_Heat_Source_By_Ms_Deepthi_Chittalury/Abstract.pdf
diff --git a/Power_Cycle_Based_On_Cold_Energy_Of_Liquefied_Natural_Gas_And_Low-Grade_Heat_Source_By_Mrs_Deepthi_Chittalury/Flowsheet.dwxml b/Power_Cycle_Based_On_Cold_Energy_Of_Lng_And_Low-Grade_Heat_Source_By_Ms_Deepthi_Chittalury/Flowsheet.dwxml
index 96cbbe4..96cbbe4 100644
--- a/Power_Cycle_Based_On_Cold_Energy_Of_Liquefied_Natural_Gas_And_Low-Grade_Heat_Source_By_Mrs_Deepthi_Chittalury/Flowsheet.dwxml
+++ b/Power_Cycle_Based_On_Cold_Energy_Of_Lng_And_Low-Grade_Heat_Source_By_Ms_Deepthi_Chittalury/Flowsheet.dwxml