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authorSashi202024-05-31 00:20:16 +0550
committerSashi202024-05-31 00:20:16 +0550
commit3ff8958795d2760c79f982ba606ef2736e87440b (patch)
tree917e9d3ddfc1aa608e1401ff25b06e837e6ea0a3
parent98752264fa05387444126e19d06fd5c00752311b (diff)
downloadDWSIM-Flowsheets-3ff8958795d2760c79f982ba606ef2736e87440b.tar.gz
DWSIM-Flowsheets-3ff8958795d2760c79f982ba606ef2736e87440b.tar.bz2
DWSIM-Flowsheets-3ff8958795d2760c79f982ba606ef2736e87440b.zip
Added(A)/Deleted(D) following Flowsheet file
D Acetylene_From_Calcium_Carbide_By_Mr_Divy_Vankar_/user_defined_compound/Merged_document.zip D Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2 D Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Abstract.pdf D Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Flowsheet.dwxmz D Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Abstract.pdf D Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Flowsheet.dwxmz D Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/user_defined_compound/Coke.json D Nitric_Acid_Dehydration_Using_Sulfuric_Acid_As_A_Solvent_By_Mr_Rohit_Chandrashekhar_Kawade/user_defined_compound/Sulfuric_acid.json D Process_Design_Of_Methyl_Chloride_Plant_By_Chlorination_Of_Methane_By_Mr_Mohanraj.g/user_defined_compound/User_defined_compounds.zip D "Process_Simulation_Of_Biodiesel_Production_From_Vegetable_Oil_Deodorization_Distillate_\r\nUsing_Hydrotalcite-Hydroxyapatite_As_A_Catalyst_By_Ms_Adithi_G_R/user_defined_compound/compounds.zip" D Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json D Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json D Production_Of_Hydrogen_Via_Biomass_Gasification_By_Mr_Yash_Misra/user_defined_compound/carbon.json
-rw-r--r--Acetylene_From_Calcium_Carbide_By_Mr_Divy_Vankar_/user_defined_compound/Merged_document.zipbin12505 -> 0 bytes
-rw-r--r--Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2386
-rw-r--r--Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Abstract.pdfbin149150 -> 0 bytes
-rw-r--r--Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Flowsheet.dwxmzbin70084 -> 0 bytes
-rw-r--r--Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Abstract.pdfbin306100 -> 0 bytes
-rw-r--r--Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Flowsheet.dwxmzbin106348 -> 0 bytes
-rw-r--r--Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/user_defined_compound/Coke.json200
-rw-r--r--Nitric_Acid_Dehydration_Using_Sulfuric_Acid_As_A_Solvent_By_Mr_Rohit_Chandrashekhar_Kawade/user_defined_compound/Sulfuric_acid.json199
-rw-r--r--Process_Design_Of_Methyl_Chloride_Plant_By_Chlorination_Of_Methane_By_Mr_Mohanraj.g/user_defined_compound/User_defined_compounds.zipbin3183 -> 0 bytes
-rw-r--r--Process_Simulation_Of_Biodiesel_Production_From_Vegetable_Oil_Deodorization_Distillate_ Using_Hydrotalcite-Hydroxyapatite_As_A_Catalyst_By_Ms_Adithi_G_R/user_defined_compound/compounds.zipbin7046 -> 0 bytes
-rw-r--r--Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json192
-rw-r--r--Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json204
-rw-r--r--Production_Of_Hydrogen_Via_Biomass_Gasification_By_Mr_Yash_Misra/user_defined_compound/carbon.json199
13 files changed, 0 insertions, 1380 deletions
diff --git a/Acetylene_From_Calcium_Carbide_By_Mr_Divy_Vankar_/user_defined_compound/Merged_document.zip b/Acetylene_From_Calcium_Carbide_By_Mr_Divy_Vankar_/user_defined_compound/Merged_document.zip
deleted file mode 100644
index 8859440..0000000
--- a/Acetylene_From_Calcium_Carbide_By_Mr_Divy_Vankar_/user_defined_compound/Merged_document.zip
+++ /dev/null
Binary files differ
diff --git a/Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2 b/Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2
deleted file mode 100644
index 04f2d13..0000000
--- a/Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2
+++ /dev/null
@@ -1,386 +0,0 @@
-{
- "Filename": "C:\\Users\\mridu\\OneDrive\\Documents\\OctaSulfur.dwcsd2",
- "cp": {
- "Acentric_Factor": 0.25,
- "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": "10544-50-0",
- "Chao_Seader_Acentricity": 0.0,
- "Chao_Seader_Liquid_Molar_Volume": 0.0,
- "Chao_Seader_Solubility_Parameter": 0.0,
- "Charge": 0,
- "ChemicalStructure": "",
- "Comments": "",
- "CompCreatorStudyFile": "C:\\Users\\mridu\\OneDrive\\Documents\\OctaSulfur.dwcsd2",
- "COSMODBName": null,
- "Critical_Compressibility": 0.26,
- "Critical_Pressure": 18208000.0,
- "Critical_Temperature": 1039.85,
- "Critical_Volume": 0.0,
- "CurrentDB": "User",
- "Dipole_Moment": 0.0,
- "Electrolyte_Cp0": 0.0,
- "Electrolyte_DelGF": 0.0,
- "Electrolyte_DelHF": 0.0,
- "EnthalpyOfFusionAtTf": 0.0,
- "Formula": "",
- "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": 38002,
- "Ideal_Gas_Heat_Capacity_Const_A": 0.70431038515,
- "Ideal_Gas_Heat_Capacity_Const_B": 0.00748085139,
- "Ideal_Gas_Heat_Capacity_Const_C": -0.00202763917,
- "Ideal_Gas_Heat_Capacity_Const_D": 0.00017306252,
- "Ideal_Gas_Heat_Capacity_Const_E": -0.00884981677,
- "IdealgasCpEquation": "6",
- "IG_Enthalpy_of_Formation_25C": 0.0,
- "IG_Entropy_of_Formation_25C": 0.0,
- "IG_Gibbs_Energy_of_Formation_25C": 0.0,
- "InChI": "",
- "Ion_CpAq_a": 0.0,
- "Ion_CpAq_b": 0.0,
- "Ion_CpAq_c": 0.0,
- "IsBlackOil": false,
- "IsCOOLPROPSupported": false,
- "IsFPROPSSupported": false,
- "IsHydratedSalt": false,
- "IsHYPO": 0,
- "IsIon": false,
- "IsModified": false,
- "IsPF": 0,
- "IsSalt": false,
- "Liquid_Density_Const_A": 0.0,
- "Liquid_Density_Const_B": 0.0,
- "Liquid_Density_Const_C": 0.0,
- "Liquid_Density_Const_D": 0.0,
- "Liquid_Density_Const_E": 0.0,
- "Liquid_Density_Tmax": 0.0,
- "Liquid_Density_Tmin": 0.0,
- "Liquid_Heat_Capacity_Const_A": 0.0,
- "Liquid_Heat_Capacity_Const_B": 0.0,
- "Liquid_Heat_Capacity_Const_C": 0.0,
- "Liquid_Heat_Capacity_Const_D": 0.0,
- "Liquid_Heat_Capacity_Const_E": 0.0,
- "Liquid_Heat_Capacity_Tmax": 0.0,
- "Liquid_Heat_Capacity_Tmin": 0.0,
- "Liquid_Thermal_Conductivity_Const_A": 0.0,
- "Liquid_Thermal_Conductivity_Const_B": 0.0,
- "Liquid_Thermal_Conductivity_Const_C": 0.0,
- "Liquid_Thermal_Conductivity_Const_D": 0.0,
- "Liquid_Thermal_Conductivity_Const_E": 0.0,
- "Liquid_Thermal_Conductivity_Tmax": 0.0,
- "Liquid_Thermal_Conductivity_Tmin": 0.0,
- "Liquid_Viscosity_Const_A": 0.0,
- "Liquid_Viscosity_Const_B": 0.0,
- "Liquid_Viscosity_Const_C": 0.0,
- "Liquid_Viscosity_Const_D": 0.0,
- "Liquid_Viscosity_Const_E": 0.0,
- "LiquidDensityEquation": "0",
- "LiquidHeatCapacityEquation": "0",
- "LiquidThermalConductivityEquation": "0",
- "LiquidViscosityEquation": "0",
- "Molar_Weight": 256.52,
- "MolarVolume_k1i": 0.0,
- "MolarVolume_k2i": 0.0,
- "MolarVolume_k3i": 0.0,
- "MolarVolume_v2i": 0.0,
- "MolarVolume_v3i": 0.0,
- "Name": "Octa-sulfur ",
- "NBP": null,
- "NegativeIon": "",
- "NegativeIonStoichCoeff": 0,
- "Normal_Boiling_Point": 614.8,
- "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": "S1SSSSSSS1",
- "Solid_Density_Const_A": 38.1305317375589,
- "Solid_Density_Const_B": -0.005,
- "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": "2",
- "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": 0.0,
- "UNIQUAC_Q": 0.0,
- "UNIQUAC_R": 0.0,
- "Vapor_Pressure_Constant_A": 0.0,
- "Vapor_Pressure_Constant_B": 0.0,
- "Vapor_Pressure_Constant_C": 0.0,
- "Vapor_Pressure_Constant_D": 0.0,
- "Vapor_Pressure_Constant_E": 0.0,
- "Vapor_Pressure_TMAX": 0.0,
- "Vapor_Pressure_TMIN": 0.0,
- "Vapor_Thermal_Conductivity_Const_A": 0.0,
- "Vapor_Thermal_Conductivity_Const_B": 0.0,
- "Vapor_Thermal_Conductivity_Const_C": 0.0,
- "Vapor_Thermal_Conductivity_Const_D": 0.0,
- "Vapor_Thermal_Conductivity_Const_E": 0.0,
- "Vapor_Thermal_Conductivity_Tmax": 0.0,
- "Vapor_Thermal_Conductivity_Tmin": 0.0,
- "Vapor_Viscosity_Const_A": 0.0,
- "Vapor_Viscosity_Const_B": 0.0,
- "Vapor_Viscosity_Const_C": 0.0,
- "Vapor_Viscosity_Const_D": 0.0,
- "Vapor_Viscosity_Const_E": 0.0,
- "Vapor_Viscosity_Tmax": 0.0,
- "Vapor_Viscosity_Tmin": 0.0,
- "VaporizationEnthalpyEquation": "",
- "VaporPressureEquation": "0",
- "VaporThermalConductivityEquation": "",
- "VaporViscosityEquation": "",
- "Z_Rackett": 0.0,
- "Elements": {},
- "MODFACGroups": {},
- "NISTMODFACGroups": {},
- "UNIFACGroups": {},
- "FullerDiffusionVolume": 0.0,
- "LennardJonesDiameter": 0.0,
- "LennardJonesEnergy": 0.0,
- "Parachor": 0.0,
- "Tag": "",
- "ExtraProperties": {},
- "COSTALD_SRK_Acentric_Factor": 0.0,
- "COSTALD_Characteristic_Volume": 0.0,
- "IsSolid": false,
- "ChemSepFamily": 1000
- },
- "database": "",
- "su": {
- "accel": "m2/s",
- "activity": "Pa",
- "activityCoefficient": "-",
- "area": "m2",
- "cakeresistance": "m/kg",
- "cinematic_viscosity": "m2/s",
- "compressibility": "1/Pa",
- "compressibilityfactor": "-",
- "deltaP": "Pa",
- "deltaT": "K.",
- "density": "kg/m3",
- "diameter": "mm",
- "distance": "m",
- "enthalpy": "kJ/kg",
- "entropy": "kJ/[kg.K]",
- "excessEnthalpy": "kJ/kg",
- "excessEntropy": "kJ/[kg.K]",
- "force": "N",
- "foulingfactor": "K.m2/W",
- "fugacity": "Pa",
- "fugacityCoefficient": "-",
- "gor": "m3/m3",
- "head": "m",
- "heat_transf_coeff": "W/[m2.K]",
- "heatCapacityCp": "kJ/[kg.K]",
- "heatCapacityCv": "kJ/[kg.K]",
- "heatflow": "kW",
- "idealGasHeatCapacity": "kJ/[kg.K]",
- "jouleThomsonCoefficient": "K/Pa",
- "kvalue": "-",
- "logfugacityCoefficient": "-",
- "logKvalue": "-",
- "mass": "kg",
- "mass_conc": "kg/m3",
- "massflow": "kg/s",
- "massfraction": "-",
- "mediumresistance": "m-1",
- "molar_conc": "mol/m3",
- "molar_enthalpy": "kJ/kmol",
- "molar_entropy": "kJ/[kmol.K]",
- "molar_volume": "m3/kmol",
- "molarflow": "mol/s",
- "molarfraction": "-",
- "molecularWeight": "kg/kmol",
- "Name": "SI",
- "pdp_boilingPointTemperature": "K",
- "pdp_meltingTemperature": "K",
- "pressure": "Pa",
- "reac_rate": "mol/[m3.s]",
- "reac_rate_heterog": "mol/[kg.s]",
- "spec_vol": "m3/kg",
- "speedOfSound": "m/s",
- "surfaceTension": "N/m",
- "temperature": "K",
- "thermalConductivity": "W/[m.K]",
- "thermalConductivityOfLiquid": "W/[m.K]",
- "thermalConductivityOfVapor": "W/[m.K]",
- "thickness": "mm",
- "time": "s",
- "vaporPressure": "Pa",
- "velocity": "m/s",
- "viscosity": "Pa.s",
- "viscosityOfLiquid": "Pa.s",
- "viscosityOfVapor": "Pa.s",
- "volume": "m3",
- "volumetricFlow": "m3/s",
- "diffusivity": "m2/s",
- "conductance": "[kg/s]/[Pa^0.5]"
- },
- "IgnoreUnsupportedGroups": false,
- "nf": "System.Globalization.NumberFormatInfo",
- "CalcMW": false,
- "CalcTC": false,
- "CalcPC": false,
- "CalcZC": false,
- "CalcZRA": true,
- "CalcAF": false,
- "CalcHF": false,
- "CalcGF": false,
- "CalcNBP": false,
- "CalcCSAF": true,
- "CalcCSSP": true,
- "CalcCSMV": true,
- "CalcMP": true,
- "CalcEM": true,
- "RegressPVAP": false,
- "RegressCPIG": false,
- "RegressCPLiquid": false,
- "RegressLVISC": false,
- "RegressLDENS": false,
- "RegressLTC": false,
- "RegressCpS": false,
- "RegressRoS": false,
- "EqPVAP": false,
- "EqCPIG": false,
- "EqCPLiquid": false,
- "EqLVISC": false,
- "EqLDENS": false,
- "EqLTC": false,
- "EqCpS": true,
- "EqSDens": false,
- "RegressOKPVAP": false,
- "RegressOKCPIG": false,
- "RegressOKCPLiquid": false,
- "RegressOKLVISC": false,
- "RegressOKLDENS": false,
- "RegressOKLTC": false,
- "RegressOKCpS": false,
- "RegressOKRoS": false,
- "ErrorMsgPVAP": "",
- "ErrorMsgCPIG": "",
- "ErrorMsgCPLiquid": "",
- "ErrorMsgLVISC": "",
- "ErrorMsgLDENS": "",
- "ErrorMsgLTC": "",
- "ErrorMsgCpS": "",
- "ErrorMsgRoS": "",
- "JobackGroups": [],
- "DataPVAP": [],
- "DataCPIG": [
- [
- 298.0,
- 0.60658038359
- ],
- [
- 300.0,
- 0.6081397162
- ],
- [
- 400.0,
- 0.65180102916
- ],
- [
- 500.0,
- 0.67207235303
- ],
- [
- 600.0,
- 0.68337751442
- ],
- [
- 700.0,
- 0.69039451114
- ],
- [
- 800.0,
- 0.69507250896
- ],
- [
- 900.0,
- 0.69858100732
- ],
- [
- 1000.0,
- 0.70092000623
- ],
- [
- 0.0,
- 0.0
- ],
- [
- 0.0,
- 0.0
- ],
- [
- 0.0,
- 0.0
- ]
- ],
- "DataCPLiquid": [],
- "DataLVISC": [],
- "DataLDENS": [
- [
- 0.0,
- 0.0
- ]
- ],
- "DataLTC": [],
- "DataCpS": [],
- "DataRoS": [
- [
- 298.15,
- 7.8239513488227042
- ]
- ],
- "AdditionalAtoms": []
-} \ No newline at end of file
diff --git a/Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Abstract.pdf b/Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Abstract.pdf
deleted file mode 100644
index e3563f6..0000000
--- a/Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Abstract.pdf
+++ /dev/null
Binary files differ
diff --git a/Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Flowsheet.dwxmz b/Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Flowsheet.dwxmz
deleted file mode 100644
index f205c4b..0000000
--- a/Laboratory_Waste_Water_Treatment_By_Supercritical_Water_Oxidation_Of_Nitrobenzene_By_Mr_Vengdhanathan_S/Flowsheet.dwxmz
+++ /dev/null
Binary files differ
diff --git a/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Abstract.pdf b/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Abstract.pdf
deleted file mode 100644
index 6c465ca..0000000
--- a/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Abstract.pdf
+++ /dev/null
Binary files differ
diff --git a/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Flowsheet.dwxmz b/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Flowsheet.dwxmz
deleted file mode 100644
index f27968c..0000000
--- a/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/Flowsheet.dwxmz
+++ /dev/null
Binary files differ
diff --git a/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/user_defined_compound/Coke.json b/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/user_defined_compound/Coke.json
deleted file mode 100644
index 56fb1ab..0000000
--- a/Manufacture_Of_Producer_Gas_By_Ms_Shreya_Singh/user_defined_compound/Coke.json
+++ /dev/null
@@ -1,200 +0,0 @@
-[
- { "unMeta": {} },
- [
- { "t": "Para", "c": [{ "t": "Str", "c": "Coke" }] },
- {
- "t": "Para",
- "c": [
- { "t": "Str", "c": "Coke" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "is" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "the" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "solid" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "residue" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "remaining" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "after" },
- { "t": "Space", "c": [] },
- { "t": "Str", "c": "certain" },
- { "t": "Space", "c": [] },
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diff --git a/Nitric_Acid_Dehydration_Using_Sulfuric_Acid_As_A_Solvent_By_Mr_Rohit_Chandrashekhar_Kawade/user_defined_compound/Sulfuric_acid.json b/Nitric_Acid_Dehydration_Using_Sulfuric_Acid_As_A_Solvent_By_Mr_Rohit_Chandrashekhar_Kawade/user_defined_compound/Sulfuric_acid.json
deleted file mode 100644
index a66f2c2..0000000
--- a/Nitric_Acid_Dehydration_Using_Sulfuric_Acid_As_A_Solvent_By_Mr_Rohit_Chandrashekhar_Kawade/user_defined_compound/Sulfuric_acid.json
+++ /dev/null
@@ -1,199 +0,0 @@
-{
- "Acentric_Factor": 1.916,
- "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": "7664-93-9",
- "Chao_Seader_Acentricity": 0.0,
- "Chao_Seader_Liquid_Molar_Volume": 0.0,
- "Chao_Seader_Solubility_Parameter": 0.0,
- "Charge": 0,
- "ChemicalStructure": "",
- "Comments": "",
- "CompCreatorStudyFile": "Y:\\OneDrive\\Arquivos DWSIM\\DWSIM 6.x Release\\Sulfuric acid.dwcsd2",
- "COSMODBName": null,
- "Critical_Compressibility": 0.0,
- "Critical_Pressure": 12942620.0,
- "Critical_Temperature": 590.76,
- "Critical_Volume": 0.2,
- "CurrentDB": "User",
- "Dipole_Moment": 0.0,
- "Electrolyte_Cp0": 0.0,
- "Electrolyte_DelGF": 0.0,
- "Electrolyte_DelHF": 0.0,
- "EnthalpyOfFusionAtTf": 15.31,
- "Formula": "H2O4S",
- "HVap_A": 711.09886468502521,
- "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": 501916,
- "Ideal_Gas_Heat_Capacity_Const_A": 13109.909650724,
- "Ideal_Gas_Heat_Capacity_Const_B": 333.840023413452,
- "Ideal_Gas_Heat_Capacity_Const_C": -0.386801452105353,
- "Ideal_Gas_Heat_Capacity_Const_D": 0.000222042675616284,
- "Ideal_Gas_Heat_Capacity_Const_E": -4.9555817463096E-08,
- "IdealgasCpEquation": "5",
- "IG_Enthalpy_of_Formation_25C": -8168.23001631321,
- "IG_Entropy_of_Formation_25C": 0.0,
- "IG_Gibbs_Energy_of_Formation_25C": -8085.84828711256,
- "InChI": "1S/H2O4S/c1-5(2,3)4/h(H2,1,2,3,4)",
- "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": 98.08,
- "MolarVolume_k1i": 0.0,
- "MolarVolume_k2i": 0.0,
- "MolarVolume_k3i": 0.0,
- "MolarVolume_v2i": 0.0,
- "MolarVolume_v3i": 0.0,
- "Name": "Sulfuric acid",
- "NBP": 431.54,
- "NegativeIon": "",
- "NegativeIonStoichCoeff": 0,
- "Normal_Boiling_Point": 431.54,
- "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=S(=O)(O)O",
- "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": 249.96,
- "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": 249.96,
- "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": 249.96,
- "UNIQUAC_Q": 0.0,
- "UNIQUAC_R": 0.0,
- "Vapor_Pressure_Constant_A": -11.08316,
- "Vapor_Pressure_Constant_B": -13587.55,
- "Vapor_Pressure_Constant_C": 96.59036,
- "Vapor_Pressure_Constant_D": 4.114803E-06,
- "Vapor_Pressure_Constant_E": 0.0,
- "Vapor_Pressure_TMAX": 578.15,
- "Vapor_Pressure_TMIN": 419.15,
- "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": "ln(Pvp) = A*ln(T) + B/T + C + D*T^2 where Pvp in kPa, T in K",
- "VaporThermalConductivityEquation": "",
- "VaporViscosityEquation": "",
- "Z_Rackett": 0.0,
- "Elements": {
- "H": 2.0,
- "O": 4.0,
- "S": 1.0
- },
- "MODFACGroups": {},
- "NISTMODFACGroups": {},
- "UNIFACGroups": {},
- "FullerDiffusionVolume": 0.0,
- "LennardJonesDiameter": 0.0,
- "LennardJonesEnergy": 0.0,
- "Parachor": 0.0,
- "Tag": "",
- "ExtraProperties": {},
- "COSTALD_SRK_Acentric_Factor": 0.0,
- "COSTALD_Characteristic_Volume": 0.0,
- "IsSolid": false,
- "ChemSepFamily": 1000
-} \ No newline at end of file
diff --git a/Process_Design_Of_Methyl_Chloride_Plant_By_Chlorination_Of_Methane_By_Mr_Mohanraj.g/user_defined_compound/User_defined_compounds.zip b/Process_Design_Of_Methyl_Chloride_Plant_By_Chlorination_Of_Methane_By_Mr_Mohanraj.g/user_defined_compound/User_defined_compounds.zip
deleted file mode 100644
index f78bd3a..0000000
--- a/Process_Design_Of_Methyl_Chloride_Plant_By_Chlorination_Of_Methane_By_Mr_Mohanraj.g/user_defined_compound/User_defined_compounds.zip
+++ /dev/null
Binary files differ
diff --git a/Process_Simulation_Of_Biodiesel_Production_From_Vegetable_Oil_Deodorization_Distillate_ Using_Hydrotalcite-Hydroxyapatite_As_A_Catalyst_By_Ms_Adithi_G_R/user_defined_compound/compounds.zip b/Process_Simulation_Of_Biodiesel_Production_From_Vegetable_Oil_Deodorization_Distillate_ Using_Hydrotalcite-Hydroxyapatite_As_A_Catalyst_By_Ms_Adithi_G_R/user_defined_compound/compounds.zip
deleted file mode 100644
index 34ad5ad..0000000
--- a/Process_Simulation_Of_Biodiesel_Production_From_Vegetable_Oil_Deodorization_Distillate_ Using_Hydrotalcite-Hydroxyapatite_As_A_Catalyst_By_Ms_Adithi_G_R/user_defined_compound/compounds.zip
+++ /dev/null
Binary files differ
diff --git a/Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json b/Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json
deleted file mode 100644
index f8c305d..0000000
--- a/Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json
+++ /dev/null
@@ -1,192 +0,0 @@
-{
- "Acentric_Factor": 0.35341443206030376,
- "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": "106-93-4",
- "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": 0.34308024518191194,
- "Critical_Pressure": 7153545.0,
- "Critical_Temperature": 588.28785057862422,
- "Critical_Volume": 0.2715,
- "CurrentDB": "User",
- "Dipole_Moment": 0.0,
- "Electrolyte_Cp0": 0.0,
- "Electrolyte_DelGF": 0.0,
- "Electrolyte_DelHF": 0.0,
- "EnthalpyOfFusionAtTf": 11.505999999999998,
- "Formula": "C2H4Br2",
- "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": 781209,
- "Ideal_Gas_Heat_Capacity_Const_A": 17452.000000000004,
- "Ideal_Gas_Heat_Capacity_Const_B": 270.2,
- "Ideal_Gas_Heat_Capacity_Const_C": -0.2278,
- "Ideal_Gas_Heat_Capacity_Const_D": 8.0800000000000012E-05,
- "Ideal_Gas_Heat_Capacity_Const_E": 0.0,
- "IdealgasCpEquation": "4",
- "IG_Enthalpy_of_Formation_25C": -170.07164833760956,
- "IG_Entropy_of_Formation_25C": 0.0,
- "IG_Gibbs_Energy_of_Formation_25C": -1439000.0,
- "InChI": "",
- "Ion_CpAq_a": 0.0,
- "Ion_CpAq_b": 0.0,
- "Ion_CpAq_c": 0.0,
- "IsBlackOil": false,
- "IsCOOLPROPSupported": false,
- "IsFPROPSSupported": false,
- "IsHydratedSalt": false,
- "IsHYPO": 0,
- "IsIon": false,
- "IsModified": false,
- "IsPF": 0,
- "IsSalt": false,
- "Liquid_Density_Const_A": 0.0,
- "Liquid_Density_Const_B": 0.0,
- "Liquid_Density_Const_C": 0.0,
- "Liquid_Density_Const_D": 0.0,
- "Liquid_Density_Const_E": 0.0,
- "Liquid_Density_Tmax": 0.0,
- "Liquid_Density_Tmin": 0.0,
- "Liquid_Heat_Capacity_Const_A": 0.0,
- "Liquid_Heat_Capacity_Const_B": 0.0,
- "Liquid_Heat_Capacity_Const_C": 0.0,
- "Liquid_Heat_Capacity_Const_D": 0.0,
- "Liquid_Heat_Capacity_Const_E": 0.0,
- "Liquid_Heat_Capacity_Tmax": 0.0,
- "Liquid_Heat_Capacity_Tmin": 0.0,
- "Liquid_Thermal_Conductivity_Const_A": 0.0,
- "Liquid_Thermal_Conductivity_Const_B": 0.0,
- "Liquid_Thermal_Conductivity_Const_C": 0.0,
- "Liquid_Thermal_Conductivity_Const_D": 0.0,
- "Liquid_Thermal_Conductivity_Const_E": 0.0,
- "Liquid_Thermal_Conductivity_Tmax": 0.0,
- "Liquid_Thermal_Conductivity_Tmin": 0.0,
- "Liquid_Viscosity_Const_A": 0.0,
- "Liquid_Viscosity_Const_B": 0.0,
- "Liquid_Viscosity_Const_C": 0.0,
- "Liquid_Viscosity_Const_D": 0.0,
- "Liquid_Viscosity_Const_E": 0.0,
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- "PositiveIonStoichCoeff": 0,
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- "SMILES": "",
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- "Solid_Heat_Capacity_Tmin": 0.0,
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- "SolidTs": 0.0,
- "SRK_Volume_Translation_Coefficient": 0.0,
- "StandardStateMolarVolume": 0.0,
- "StoichSum": 0,
- "Surface_Tension_Const_A": 0.0,
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- "Surface_Tension_Tmax": 0.0,
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- "SurfaceTensionEquation": "",
- "TemperatureOfFusion": 231.9,
- "UNIQUAC_Q": 0.0,
- "UNIQUAC_R": 0.0,
- "Vapor_Pressure_Constant_A": 0.0,
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- "Vapor_Viscosity_Const_C": 0.0,
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- "Vapor_Viscosity_Const_E": 0.0,
- "Vapor_Viscosity_Tmax": 0.0,
- "Vapor_Viscosity_Tmin": 0.0,
- "VaporizationEnthalpyEquation": "",
- "VaporPressureEquation": "",
- "VaporThermalConductivityEquation": "",
- "VaporViscosityEquation": "",
- "Z_Rackett": 0.34308024518191194,
- "Elements": {},
- "MODFACGroups": {},
- "NISTMODFACGroups": {},
- "UNIFACGroups": {
- "2": 2,
- "65": 2
- },
- "FullerDiffusionVolume": 0.0,
- "LennardJonesDiameter": 0.0,
- "LennardJonesEnergy": 0.0,
- "Parachor": 0.0
-} \ No newline at end of file
diff --git a/Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json b/Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json
deleted file mode 100644
index 80e0ab6..0000000
--- a/Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json
+++ /dev/null
@@ -1,204 +0,0 @@
-{
- "Acentric_Factor": 0.7,
- "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": "64-18-6",
- "Chao_Seader_Acentricity": 0.7,
- "Chao_Seader_Liquid_Molar_Volume": 46.3,
- "Chao_Seader_Solubility_Parameter": 14.26,
- "Charge": 0,
- "ChemicalStructure": "",
- "Comments": "",
- "CompCreatorStudyFile": "C:\\Users\\DELL\\Documents\\IQ\\Asesoría\\Tesis\\Formic Acid.dwcsd2",
- "COSMODBName": null,
- "Critical_Compressibility": 0.22,
- "Critical_Pressure": 7587806.09,
- "Critical_Temperature": 588.0,
- "Critical_Volume": 0.0,
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- "Dipole_Moment": 0.0,
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- "Electrolyte_DelGF": 0.0,
- "Electrolyte_DelHF": 0.0,
- "EnthalpyOfFusionAtTf": 12.68,
- "Formula": "O2H2C",
- "HVap_A": 0.0,
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- "ID": 79107,
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- "Ideal_Gas_Heat_Capacity_Const_B": 107.3,
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- "Ideal_Gas_Heat_Capacity_Const_E": 0.0,
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- "IG_Gibbs_Energy_of_Formation_25C": -6057.58,
- "InChI": "",
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- "Ion_CpAq_b": 0.0,
- "Ion_CpAq_c": 0.0,
- "IsBlackOil": false,
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- "IsIon": false,
- "IsModified": false,
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- "Liquid_Density_Const_C": 0.0,
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- "Liquid_Thermal_Conductivity_Const_B": 0.0,
- "Liquid_Thermal_Conductivity_Const_C": 0.0,
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- "MolarVolume_v2i": 0.0,
- "MolarVolume_v3i": 0.0,
- "Name": "Formic Acid",
- "NBP": null,
- "NegativeIon": "",
- "NegativeIonStoichCoeff": 0,
- "Normal_Boiling_Point": 363.32,
- "OriginalDB": "User",
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- "PF_v2": null,
- "PF_vA": null,
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- "PositiveIon": "",
- "PositiveIonStoichCoeff": 0,
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- "Surface_Tension_Tmax": 0.0,
- "Surface_Tension_Tmin": 0.0,
- "SurfaceTensionEquation": "",
- "TemperatureOfFusion": 203.85,
- "UNIQUAC_Q": 0.0,
- "UNIQUAC_R": 0.0,
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- "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": 0.22,
- "Elements": {
- "C": 1,
- "H": 2,
- "O": 2
- },
- "MODFACGroups": {
- "43": "1"
- },
- "NISTMODFACGroups": {
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- },
- "UNIFACGroups": {
- "44": "1"
- },
- "FullerDiffusionVolume": 0.0,
- "LennardJonesDiameter": 0.0,
- "LennardJonesEnergy": 0.0,
- "Parachor": 0.0,
- "Tag": "",
- "ExtraProperties": {},
- "COSTALD_SRK_Acentric_Factor": 0.0,
- "COSTALD_Characteristic_Volume": 0.0,
- "IsSolid": false
-} \ No newline at end of file
diff --git a/Production_Of_Hydrogen_Via_Biomass_Gasification_By_Mr_Yash_Misra/user_defined_compound/carbon.json b/Production_Of_Hydrogen_Via_Biomass_Gasification_By_Mr_Yash_Misra/user_defined_compound/carbon.json
deleted file mode 100644
index 862519e..0000000
--- a/Production_Of_Hydrogen_Via_Biomass_Gasification_By_Mr_Yash_Misra/user_defined_compound/carbon.json
+++ /dev/null
@@ -1,199 +0,0 @@
-{
- "Acentric_Factor": 1.0,
- "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": "7440-44-0",
- "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": 796719000.0,
- "Critical_Temperature": 7020.5,
- "Critical_Volume": 0.027,
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- "Electrolyte_DelGF": 0.0,
- "Electrolyte_DelHF": 0.0,
- "EnthalpyOfFusionAtTf": 115.0,
- "Formula": "C",
- "HVap_A": 91163.819457268983,
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- "HVap_D": 0.0,
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- "HVap_TMIN": 0.0,
- "HydrationNumber": 0.0,
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- "Ideal_Gas_Heat_Capacity_Const_E": 0.0,
- "IdealgasCpEquation": "0",
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- "IG_Gibbs_Energy_of_Formation_25C": 55751.32,
- "InChI": "1S/C",
- "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,
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- "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,
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- "Liquid_Heat_Capacity_Tmin": 0.0,
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- "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,
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- "Liquid_Viscosity_Const_D": 0.0,
- "Liquid_Viscosity_Const_E": 0.0,
- "LiquidDensityEquation": "0",
- "LiquidHeatCapacityEquation": "0",
- "LiquidThermalConductivityEquation": "",
- "LiquidViscosityEquation": "0",
- "Molar_Weight": 12.01,
- "MolarVolume_k1i": 0.0,
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- "MolarVolume_k3i": 0.0,
- "MolarVolume_v2i": 0.0,
- "MolarVolume_v3i": 0.0,
- "Name": "Carbon",
- "NBP": 4600.0,
- "NegativeIon": "",
- "NegativeIonStoichCoeff": 0,
- "Normal_Boiling_Point": 4600.0,
- "OriginalDB": "User",
- "PC_SAFT_epsilon_k": 0.0,
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- "PF_Tv2": null,
- "PF_v1": null,
- "PF_v2": null,
- "PF_vA": null,
- "PF_vB": null,
- "PF_Watson_K": null,
- "PositiveIon": "",
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- "PR_Volume_Translation_Coefficient": 0.0,
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- "Solid_Density_Const_A": 188.9,
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- "Vapor_Viscosity_Tmax": 0.0,
- "Vapor_Viscosity_Tmin": 0.0,
- "VaporizationEnthalpyEquation": "",
- "VaporPressureEquation": "1",
- "VaporThermalConductivityEquation": "",
- "VaporViscosityEquation": "",
- "Z_Rackett": 0.3,
- "Elements": {
- "C": 1.0
- },
- "MODFACGroups": {},
- "NISTMODFACGroups": {},
- "UNIFACGroups": {
- "4": "1"
- },
- "FullerDiffusionVolume": 0.0,
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- "Parachor": 0.0,
- "Tag": "",
- "ExtraProperties": {},
- "COSTALD_SRK_Acentric_Factor": 0.0,
- "COSTALD_Characteristic_Volume": 0.0,
- "IsSolid": false,
- "ChemSepFamily": 1000
-} \ No newline at end of file