Added(A)/Deleted(D) following Flowsheet file

 A  Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Abstract.pdf
A  Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Flowsheet.dwxmz
A  Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2
R  Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Abstract.pdf -> Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Abstract.pdf
A  Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Flowsheet.dwxmz
A  Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/README.txt
A  "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"
M  Process_Simulation_Of_Steam_Stripping_Of_Bleached_Palm_Oil_Deodorization_For_Removing_Free_Fatty_Acids_By_Mr_Challa_Deepak/flowsheet.dwxmz
A  Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json
A  Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json
A  Production_Of_Heptenes_From_Propylene_And_Butenes_By_Mr_Akshay_Sunil_Karandikar/README.txt
A  Production_Of_Hydrogen_Through_A_Sulfur-Iodine_Cycle_Based_On_The_Electrochemical_Bunsen_Reaction_By_Mr_Ayush_Ramchandra_Shirodkar/user_defined_compound/sulfuricacid.json
A  Production_Of_Recombinant_Beta-Glucosidase_By_Mr_A_Arun_Kumar/user_defined_compound/User_defined_chemicals.zip
A  Production_Of_Recombinant_Cellulase_By_Ms_Akhila_S_Hegde/user_defined_compound/Compounds.zip
D  Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Flowsheet.dwxmz
A  Simulation_Of_Cellulase_Production_By_Submerged_Fermentation_Of_Trichoderma_Reesei_By_Ms_Ananya_Gb/user_defined_compound/Compounds.zip
A  Simulation_Of_Polygalacturonase_Production_By_Submerged_Fermentation_Of_Aspergillus_Carbonarius_By_Mr_Shravan_R_Shankar/user_defined_compound/user_defined_compounds.zip
A  Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Abstract.pdf
A  Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Flowsheet.dwxmz

19 files changed, 991 insertions, 0 deletions

diff --git a/Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Abstract.pdf b/Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Abstract.pdf
new file mode 100644
index 0000000..7d2285b
--- /dev/null
+++ b/Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Abstract.pdf
diff --git a/Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Flowsheet.dwxmz b/Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Flowsheet.dwxmz
new file mode 100644
index 0000000..a864494
--- /dev/null
+++ b/Closed_Cycle_Liquefaction_Of_Co2_By_Mr_Jeet_Pinkal_Doshi/Flowsheet.dwxmz
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
new file mode 100644
index 0000000..04f2d13
--- /dev/null
+++ b/Design_Of_A_Claus_Unit_For_The_Conversion_Of_Hydrogen_Sulfide_To_Elemental_Sulfur_By_Mr_Mudit_Nainani/user_defined_compound/OctaSulfur.dwcsd2
@@ -0,0 +1,386 @@
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+  },

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+  "nf": "System.Globalization.NumberFormatInfo",

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+  "EqLTC": false,

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+  "ErrorMsgCPLiquid": "",

+  "ErrorMsgLVISC": "",

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+  "ErrorMsgLTC": "",

+  "ErrorMsgCpS": "",

+  "ErrorMsgRoS": "",

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+      0.68337751442

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+      0.69039451114

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+      0.70092000623

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+    ],

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+  "DataLDENS": [

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+      0.0,

+      0.0

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+  "DataLTC": [],

+  "DataCpS": [],

+  "DataRoS": [

+    [

+      298.15,

+      7.8239513488227042

+    ]

+  ],

+  "AdditionalAtoms": []

+}
\ No newline at end of file
diff --git a/Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Abstract.pdf b/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Abstract.pdf
index a60c20b..6bbc409 100644
--- a/Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Abstract.pdf
+++ b/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Abstract.pdf
diff --git a/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Flowsheet.dwxmz b/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Flowsheet.dwxmz
new file mode 100644
index 0000000..c8b390a
--- /dev/null
+++ b/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/Flowsheet.dwxmz
diff --git a/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/README.txt b/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/README.txt
new file mode 100644
index 0000000..f6ed770
--- /dev/null
+++ b/Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal_And_Daniel_Antonio_Chuquin_Vasco/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Extractive Distillation for Separating N-Hexane and Ethyl Acetate using NMP
+Proposar Name: Ms Denisse Yajaira Chicaiza Sagal and Daniel Antonio Chuquin Vasco
+University: Escuela Superior Politécnica De Chimborazo, Riobamba, Ecuador
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
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
new file mode 100644
index 0000000..34ad5ad
--- /dev/null
+++ 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
diff --git a/Process_Simulation_Of_Steam_Stripping_Of_Bleached_Palm_Oil_Deodorization_For_Removing_Free_Fatty_Acids_By_Mr_Challa_Deepak/flowsheet.dwxmz b/Process_Simulation_Of_Steam_Stripping_Of_Bleached_Palm_Oil_Deodorization_For_Removing_Free_Fatty_Acids_By_Mr_Challa_Deepak/flowsheet.dwxmz
index 9afe99b..78d048a 100644
--- a/Process_Simulation_Of_Steam_Stripping_Of_Bleached_Palm_Oil_Deodorization_For_Removing_Free_Fatty_Acids_By_Mr_Challa_Deepak/flowsheet.dwxmz
+++ b/Process_Simulation_Of_Steam_Stripping_Of_Bleached_Palm_Oil_Deodorization_For_Removing_Free_Fatty_Acids_By_Mr_Challa_Deepak/flowsheet.dwxmz
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
new file mode 100644
index 0000000..f8c305d
--- /dev/null
+++ b/Production_Of_Ethylene_Dichloride_By_Mr_Manas_Ramdas_Pawar/user_defined_compound/Ethylene_Dibromide.json
@@ -0,0 +1,192 @@
+{

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+  "BO_SGG": 0.0,

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+  "Chao_Seader_Solubility_Parameter": 0.0,

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+  "ChemicalStructure": "",

+  "Comments": "",

+  "CompCreatorStudyFile": "",

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+  "Critical_Compressibility": 0.34308024518191194,

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+  "Ideal_Gas_Heat_Capacity_Const_E": 0.0,

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+  "SRK_Volume_Translation_Coefficient": 0.0,

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+  "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
new file mode 100644
index 0000000..80e0ab6
--- /dev/null
+++ b/Production_Of_Formic_Acid_In_A_Dividing_Wall_Reactive_Distillation_Column_By_Mr_Alexander_Bayas/user_defined_compound/FormicAcid.json
@@ -0,0 +1,204 @@
+{

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+  "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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+  "Ideal_Gas_Heat_Capacity_Const_E": 0.0,

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+  "IG_Enthalpy_of_Formation_25C": -6556.87,

+  "IG_Entropy_of_Formation_25C": 0.0,

+  "IG_Gibbs_Energy_of_Formation_25C": -6057.58,

+  "InChI": "",

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+  "Solid_Heat_Capacity_Tmax": 203.85,

+  "Solid_Heat_Capacity_Tmin": 0.0,

+  "SolidDensityAtTs": 0.0,

+  "SolidDensityEquation": "2",

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+  "Surface_Tension_Const_E": 0.0,

+  "Surface_Tension_Tmax": 0.0,

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+  "SurfaceTensionEquation": "",

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+  "Vapor_Pressure_Constant_B": 0.0,

+  "Vapor_Pressure_Constant_C": 0.0,

+  "Vapor_Pressure_Constant_D": 0.0,

+  "Vapor_Pressure_Constant_E": 0.0,

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+  "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": 0.22,

+  "Elements": {

+    "C": 1,

+    "H": 2,

+    "O": 2

+  },

+  "MODFACGroups": {

+    "43": "1"

+  },

+  "NISTMODFACGroups": {

+    "43": "1"

+  },

+  "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_Heptenes_From_Propylene_And_Butenes_By_Mr_Akshay_Sunil_Karandikar/README.txt b/Production_Of_Heptenes_From_Propylene_And_Butenes_By_Mr_Akshay_Sunil_Karandikar/README.txt
new file mode 100644
index 0000000..2f3e764
--- /dev/null
+++ b/Production_Of_Heptenes_From_Propylene_And_Butenes_By_Mr_Akshay_Sunil_Karandikar/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Production of Heptenes from Propylene and Butenes
+Proposar Name: Mr Akshay Sunil Karandikar
+University: Thadomal Shahani Engineering College
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Production_Of_Hydrogen_Through_A_Sulfur-Iodine_Cycle_Based_On_The_Electrochemical_Bunsen_Reaction_By_Mr_Ayush_Ramchandra_Shirodkar/user_defined_compound/sulfuricacid.json b/Production_Of_Hydrogen_Through_A_Sulfur-Iodine_Cycle_Based_On_The_Electrochemical_Bunsen_Reaction_By_Mr_Ayush_Ramchandra_Shirodkar/user_defined_compound/sulfuricacid.json
new file mode 100644
index 0000000..811aa69
--- /dev/null
+++ b/Production_Of_Hydrogen_Through_A_Sulfur-Iodine_Cycle_Based_On_The_Electrochemical_Bunsen_Reaction_By_Mr_Ayush_Ramchandra_Shirodkar/user_defined_compound/sulfuricacid.json
@@ -0,0 +1,193 @@
+{

+  "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": "7664-93-9",

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+  "Chao_Seader_Liquid_Molar_Volume": 0.0,

+  "Chao_Seader_Solubility_Parameter": 0.0,

+  "Charge": 0,

+  "ChemicalStructure": "",

+  "Comments": "",

+  "CompCreatorStudyFile": "C:\\Users\\aisha&ayush\\Desktop\\DWSIM\\17. Flowsheet\\sulfuric acid.dwcsd2",

+  "COSMODBName": null,

+  "Critical_Compressibility": 0.0,

+  "Critical_Pressure": 12942620.0,

+  "Critical_Temperature": 590.76,

+  "Critical_Volume": 0.0,

+  "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": 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": 86161,

+  "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": -801.14,

+  "IG_Entropy_of_Formation_25C": 0.0,

+  "IG_Gibbs_Energy_of_Formation_25C": -793.06,

+  "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": 98.07,

+  "MolarVolume_k1i": 0.0,

+  "MolarVolume_k2i": 0.0,

+  "MolarVolume_k3i": 0.0,

+  "MolarVolume_v2i": 0.0,

+  "MolarVolume_v3i": 0.0,

+  "Name": "Sulfuric acid",

+  "NBP": null,

+  "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": "",

+  "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": 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": {

+    "H": 2,

+    "O": 4,

+    "S": 1

+  },

+  "MODFACGroups": {},

+  "NISTMODFACGroups": {},

+  "UNIFACGroups": {},

+  "FullerDiffusionVolume": 0.0,

+  "LennardJonesDiameter": 0.0,

+  "LennardJonesEnergy": 0.0,

+  "Parachor": 0.0

+}
\ No newline at end of file
diff --git a/Production_Of_Recombinant_Beta-Glucosidase_By_Mr_A_Arun_Kumar/user_defined_compound/User_defined_chemicals.zip b/Production_Of_Recombinant_Beta-Glucosidase_By_Mr_A_Arun_Kumar/user_defined_compound/User_defined_chemicals.zip
new file mode 100644
index 0000000..d6a25bf
--- /dev/null
+++ b/Production_Of_Recombinant_Beta-Glucosidase_By_Mr_A_Arun_Kumar/user_defined_compound/User_defined_chemicals.zip
diff --git a/Production_Of_Recombinant_Cellulase_By_Ms_Akhila_S_Hegde/user_defined_compound/Compounds.zip b/Production_Of_Recombinant_Cellulase_By_Ms_Akhila_S_Hegde/user_defined_compound/Compounds.zip
new file mode 100644
index 0000000..8a1f410
--- /dev/null
+++ b/Production_Of_Recombinant_Cellulase_By_Ms_Akhila_S_Hegde/user_defined_compound/Compounds.zip
diff --git a/Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Flowsheet.dwxmz b/Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Flowsheet.dwxmz
deleted file mode 100644
index 03630a9..0000000
--- a/Simulation_Control_Of_Vapor_Recompression_Assisted_Extractive_Distillation_For_Separating_N-Hexane_And_Ethyl_Acetate_Using_Nmp_By_Ms_Denisse_Yajaira_Chicaiza_Sagal/Flowsheet.dwxmz
+++ /dev/null
diff --git a/Simulation_Of_Cellulase_Production_By_Submerged_Fermentation_Of_Trichoderma_Reesei_By_Ms_Ananya_Gb/user_defined_compound/Compounds.zip b/Simulation_Of_Cellulase_Production_By_Submerged_Fermentation_Of_Trichoderma_Reesei_By_Ms_Ananya_Gb/user_defined_compound/Compounds.zip
new file mode 100644
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--- /dev/null
+++ b/Simulation_Of_Cellulase_Production_By_Submerged_Fermentation_Of_Trichoderma_Reesei_By_Ms_Ananya_Gb/user_defined_compound/Compounds.zip
diff --git a/Simulation_Of_Polygalacturonase_Production_By_Submerged_Fermentation_Of_Aspergillus_Carbonarius_By_Mr_Shravan_R_Shankar/user_defined_compound/user_defined_compounds.zip b/Simulation_Of_Polygalacturonase_Production_By_Submerged_Fermentation_Of_Aspergillus_Carbonarius_By_Mr_Shravan_R_Shankar/user_defined_compound/user_defined_compounds.zip
new file mode 100644
index 0000000..7d3566a
--- /dev/null
+++ b/Simulation_Of_Polygalacturonase_Production_By_Submerged_Fermentation_Of_Aspergillus_Carbonarius_By_Mr_Shravan_R_Shankar/user_defined_compound/user_defined_compounds.zip
diff --git a/Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Abstract.pdf b/Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Abstract.pdf
new file mode 100644
index 0000000..91daad1
--- /dev/null
+++ b/Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Abstract.pdf
diff --git a/Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Flowsheet.dwxmz b/Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Flowsheet.dwxmz
new file mode 100644
index 0000000..42998c7
--- /dev/null
+++ b/Styrene_Production_With_Ethylbenzene_Recycling_By_Prof_Sandino_Michael_Angelo_G._Aguilar/Flowsheet.dwxmz