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

D Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking.dwxmz D Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking_abstract.pdf D Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/user_defined_compound/user_defined_components.zip D Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.dwxmz D Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.pdf D Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Abstract.pdf D Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Flowsheet.dwxmz D Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/abstract.pdf D Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/flowsheet.dwxmz R Multicomponent_Distillation_Of_Propane,1-Butene,n-Butane,trans-2-Butene,cis-2-Butene,and_N-Pentane_By_Mr_Meet_Dave_&_Roshan_Hirani/MultiComponentDistilation.pdf -> Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/MultiComponentDistilation.pdf R Multicomponent_Distillation_Of_Propane,1-Butene,n-Butane,trans-2-Butene,cis-2-Butene,and_N-Pentane_By_Mr_Meet_Dave_&_Roshan_Hirani/MulticompnentDistillation.dwxmz -> Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/MulticompnentDistillation.dwxmz A Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/README.txt D Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/FLOWSHEET.dwxmz D Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/abstract.pdf D Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project.pdf D Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project_ex.dwxmz D Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/Abstract.pdf D Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/WOM_Ishty_Malhotra.dwxmz D Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/user_defined_compound/NaHS.zip R Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf -> Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/Abstract.pdf R Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Flowsheet.dwxmz -> Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/Flowsheet.dwxmz A Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/README.txt A Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/README.txt A Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Abstract.pdf A Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Flowsheet.dwxmz A Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt R The_Separation_Process_Of_A_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Abstract.pdf -> Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Abstract.pdf R The_Separation_Process_Of_A_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Flowsheet.dwxmz -> Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Flowsheet.dwxmz A Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/README.txt D Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Abstract.pdf D Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Flowsheet.dwxmz D Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/Abstract.pdf D Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/PressureSwingDistillationForSeparationOfMethylAcetateMethanolAzeotropicMixture.dwxmz A Process_Development_For_The_Production_Of_100_Tpd_Dmf_Using_Methanol_Dehydrogenation_Process_By_Mr_S._Srinivasan/user_defined_compound/Dimethylamine.json D Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdf D Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmz D Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/Formaldehyde_Production.dwxmz D Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdf D Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Abstract_isobuteneProduction.pdf D Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Flowsheet_isobuteneProduction.dwxml D Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/Abstract.pdf D Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/DC_with_table.dwxmz D Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/user_defined_compound/Methyl_DiEthanolAmine.zip D Production_Of_Terepthalic_Acid_From_Oxidation_Of_P-Xylene_By_Mr_Kaushal_Sannjay_Yadav,_Ms_Riyaben_Yogeshbhai_Tailor_&_Nikunj_Shantilal_Prajapati/finalabstract.pdf D Production_Of_Terepthalic_Acid_From_Oxidation_Of_P-Xylene_By_Mr_Kaushal_Sannjay_Yadav,_Ms_Riyaben_Yogeshbhai_Tailor_&_Nikunj_Shantilal_Prajapati/finalrun.dwxml A Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Abstarct_Flowsheet_submission.pdf A Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Propane_Propylene_MVR.dwxmz A Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/README.txt D Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionabstractconverted.pdf D Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionprocessfortherecoveryoffreshwater.dwxmz D Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Group_9_Simulation_Description.pdf D Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Sulfuric_acid_process_GroupAtul.dwxmz A Synthesis_Of_Ammonia_In_Cryogenic_Process_By_Mr_Yash_Shankar_Chikorde/README.txt D Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Abstract_Ethanol.pdf D Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Ethanol_Flowsheet.dwxmz D Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.dwxmz D Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.pdf D Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/Abstract_tcpsed.pdf D Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/triple_column_pressureswing_with_extractive_distillation.dwxmz
author: Sashi20 2021-12-16 00:20:14 +0550
committer: Sashi20 2021-12-16 00:20:14 +0550
commit: 09bbc1651ae4ec837399f820ead3ca445b0bd31e (patch)
tree: 851610cec92a2eff5aa07388ff86fda72a0f4ce7
parent: 02b340799399458167d550feee1286978aeda61b (diff)
download: DWSIM-Flowsheets-09bbc1651ae4ec837399f820ead3ca445b0bd31e.tar.gz
DWSIM-Flowsheets-09bbc1651ae4ec837399f820ead3ca445b0bd31e.tar.bz2
DWSIM-Flowsheets-09bbc1651ae4ec837399f820ead3ca445b0bd31e.zip
59 files changed, 260 insertions, 41094 deletions
diff --git a/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking.dwxmz b/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking.dwxmz
deleted file mode 100644
index 929c92e..0000000
--- a/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking.dwxmz
+++ /dev/null
diff --git a/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking_abstract.pdf b/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking_abstract.pdf
deleted file mode 100644
index 872dc2a..0000000
--- a/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/cumene_cracking_abstract.pdf
+++ /dev/null
diff --git a/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/user_defined_compound/user_defined_components.zip b/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/user_defined_compound/user_defined_components.zip
deleted file mode 100644
index 4335801..0000000
--- a/Acetone_phenol_Production_Via_Cumene_Cracking_By_Mr_Aarsh_Dodhia/user_defined_compound/user_defined_components.zip
+++ /dev/null
diff --git a/Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.dwxmz b/Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.dwxmz
deleted file mode 100644
index f1269e4..0000000
--- a/Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.dwxmz
+++ /dev/null
diff --git a/Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.pdf b/Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.pdf
deleted file mode 100644
index 1619064..0000000
--- a/Ammonia_Water_Distillation_By_Mr_Malapati_Sree_Harsha/dist_aq_ammonia.pdf
+++ /dev/null
diff --git a/Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Abstract.pdf b/Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Abstract.pdf
deleted file mode 100644
index 2ac557d..0000000
--- a/Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Abstract.pdf
+++ /dev/null
diff --git a/Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Flowsheet.dwxmz b/Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Flowsheet.dwxmz
deleted file mode 100644
index 5fec2b3..0000000
--- a/Dehydration_Of_Thf_By_Pressure_Swing_Distillation_By_Mr_Dev_Parihar_And_Yash_Parmar/Flowsheet.dwxmz
+++ /dev/null
diff --git a/Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/abstract.pdf b/Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/abstract.pdf
deleted file mode 100644
index 2e2e840..0000000
--- a/Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/abstract.pdf
+++ /dev/null
diff --git a/Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/flowsheet.dwxmz b/Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/flowsheet.dwxmz
deleted file mode 100644
index a215ca6..0000000
--- a/Depropanizer_For_Natural_Gas_Liquids_By_Ms_Yekkaluri_Snehasree_Reddy/flowsheet.dwxmz
+++ /dev/null
diff --git a/Multicomponent_Distillation_Of_Propane,1-Butene,n-Butane,trans-2-Butene,cis-2-Butene,and_N-Pentane_By_Mr_Meet_Dave_&_Roshan_Hirani/MultiComponentDistilation.pdf b/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/MultiComponentDistilation.pdf
index 4cce895..4cce895 100644
--- a/Multicomponent_Distillation_Of_Propane,1-Butene,n-Butane,trans-2-Butene,cis-2-Butene,and_N-Pentane_By_Mr_Meet_Dave_&_Roshan_Hirani/MultiComponentDistilation.pdf
+++ b/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/MultiComponentDistilation.pdf
diff --git a/Multicomponent_Distillation_Of_Propane,1-Butene,n-Butane,trans-2-Butene,cis-2-Butene,and_N-Pentane_By_Mr_Meet_Dave_&_Roshan_Hirani/MulticompnentDistillation.dwxmz b/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/MulticompnentDistillation.dwxmz
index fff91de..fff91de 100644
--- a/Multicomponent_Distillation_Of_Propane,1-Butene,n-Butane,trans-2-Butene,cis-2-Butene,and_N-Pentane_By_Mr_Meet_Dave_&_Roshan_Hirani/MulticompnentDistillation.dwxmz
+++ b/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/MulticompnentDistillation.dwxmz
diff --git a/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/README.txt b/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/README.txt
new file mode 100644
index 0000000..4dc2059
--- /dev/null
+++ b/Distillation_Trains_For_Paraffin_Separation_By_Mr_Meet_Dave_&_Roshan_Hirani/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Distillation Trains for Paraffin Separation
+Proposar Name: Mr Meet Dave & Roshan Hirani
+University: G H Patel College of Engineering & Technology, Vallabh Vidyanagar
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/FLOWSHEET.dwxmz b/Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/FLOWSHEET.dwxmz
deleted file mode 100644
index 1713fac..0000000
--- a/Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/FLOWSHEET.dwxmz
+++ /dev/null
diff --git a/Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/abstract.pdf b/Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/abstract.pdf
deleted file mode 100644
index f078312..0000000
--- a/Ethylene_Production_Via_Cracking_Of_Ethane-Propane_By_Ms_Shivashree_Asthana/abstract.pdf
+++ /dev/null
diff --git a/Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project.pdf b/Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project.pdf
deleted file mode 100644
index 0fd9fad..0000000
--- a/Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project.pdf
+++ /dev/null
diff --git a/Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project_ex.dwxmz b/Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project_ex.dwxmz
deleted file mode 100644
index ba5447f..0000000
--- a/Extractive-Distillation_Methods_For_Methanol-Recovery_Systems_In_The_Tame_Reactive-Distillation_Process_By_Mr_Harsh_Srivastava/tame_project_ex.dwxmz
+++ /dev/null
diff --git a/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/Abstract.pdf b/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/Abstract.pdf
deleted file mode 100644
index fa1397a..0000000
--- a/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/Abstract.pdf
+++ /dev/null
diff --git a/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/WOM_Ishty_Malhotra.dwxmz b/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/WOM_Ishty_Malhotra.dwxmz
deleted file mode 100644
index 485259d..0000000
--- a/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/WOM_Ishty_Malhotra.dwxmz
+++ /dev/null
diff --git a/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/user_defined_compound/NaHS.zip b/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/user_defined_compound/NaHS.zip
deleted file mode 100644
index 1acc27c..0000000
--- a/Industrial_Spent_Caustic_Wastewater_Treatment_By_Wet_Oxidation_Method_By_Ms_Ishty_Malhotra/user_defined_compound/NaHS.zip
+++ /dev/null
diff --git a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/Abstract.pdf
index 139f804..139f804 100644
--- a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Abstract.pdf
+++ b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/Abstract.pdf
diff --git a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Flowsheet.dwxmz b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/Flowsheet.dwxmz
index 3514366..3514366 100644
--- a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_Adapted_By_Mr_Dineshkumar/Flowsheet.dwxmz
+++ b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/Flowsheet.dwxmz
diff --git a/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/README.txt b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/README.txt
new file mode 100644
index 0000000..e6ef871
--- /dev/null
+++ b/Isopropyl_Alcohol_Synthesis_From_Propylene_And_Water_By_Mr_M_Dineshkumar/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Isopropyl Alcohol synthesis from Propylene and Water
+Proposar Name: Mr Dineshkumar
+University: Anjalai Ammal Mahalingam Engineering College,Koilvenni
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/README.txt b/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/README.txt
new file mode 100644
index 0000000..7d24c5e
--- /dev/null
+++ b/Methane_Liquefaction_Cycle_By_Ms_Preethi_Para/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Methane Liquefaction Cycle
+Proposar Name: Ms Preethi Para
+University: National Institute of Technology Rourkela
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Abstract.pdf b/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Abstract.pdf
new file mode 100644
index 0000000..019330d
--- /dev/null
+++ b/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Abstract.pdf
diff --git a/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Flowsheet.dwxmz b/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Flowsheet.dwxmz
new file mode 100644
index 0000000..fc92dab
--- /dev/null
+++ b/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/Flowsheet.dwxmz
diff --git a/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt b/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt
new file mode 100644
index 0000000..d61a513
--- /dev/null
+++ b/Monochlorobenzene_Separation_Process_By_Ms_Ana_Paula_Ribeiro_Paiva/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: MonoChlorobenzene Separation Process
+Proposar Name: Ms Ana Paula Ribeiro Paiva
+University: Universidade Federal Fluminense, Rio de Janeiro
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/The_Separation_Process_Of_A_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Abstract.pdf b/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Abstract.pdf
index f7694f3..f7694f3 100644
--- a/The_Separation_Process_Of_A_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Abstract.pdf
+++ b/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Abstract.pdf
diff --git a/The_Separation_Process_Of_A_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Flowsheet.dwxmz b/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Flowsheet.dwxmz
index 13afa1f..13afa1f 100644
--- a/The_Separation_Process_Of_A_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Flowsheet.dwxmz
+++ b/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/Flowsheet.dwxmz
diff --git a/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/README.txt b/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/README.txt
new file mode 100644
index 0000000..60ae050
--- /dev/null
+++ b/Pressure-Swing_Distillation_For_Separation_Of_Maximum_Boiling_Azeotropic_System_Of_Water_And_Eda_By_Mr_B_Siddharth_And_Sharmistha_Lochan_Gupta/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Pressure-Swing Distillation for Separation of Maximum Boiling Azeotropic System of Water and EDA
+Proposar Name: Mr B Siddharth And Sharmistha Lochan Gupta
+University: University School of Chemical Technology, GGSIPU
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Abstract.pdf b/Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Abstract.pdf
deleted file mode 100644
index 9b83b3e..0000000
--- a/Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Abstract.pdf
+++ /dev/null
diff --git a/Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Flowsheet.dwxmz b/Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Flowsheet.dwxmz
deleted file mode 100644
index 7f00a47..0000000
--- a/Pressure-Swing_Reactive_Distillation_Method_For_Production_Of_N-Propyl_Acetate_By_Ms_Chandni/Flowsheet.dwxmz
+++ /dev/null
diff --git a/Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/Abstract.pdf b/Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/Abstract.pdf
deleted file mode 100644
index 1bf4214..0000000
--- a/Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/Abstract.pdf
+++ /dev/null
diff --git a/Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/PressureSwingDistillationForSeparationOfMethylAcetateMethanolAzeotropicMixture.dwxmz b/Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/PressureSwingDistillationForSeparationOfMethylAcetateMethanolAzeotropicMixture.dwxmz
deleted file mode 100644
index 3ffabac..0000000
--- a/Pressure_Swing_Distillation_For_The_Separation_Of_Methyl_Acetate-Methanol_Azeotrope_By_Mr_Prajwal_Sharad_Thakare/PressureSwingDistillationForSeparationOfMethylAcetateMethanolAzeotropicMixture.dwxmz
+++ /dev/null
diff --git a/Process_Development_For_The_Production_Of_100_Tpd_Dmf_Using_Methanol_Dehydrogenation_Process_By_Mr_S._Srinivasan/user_defined_compound/Dimethylamine.json b/Process_Development_For_The_Production_Of_100_Tpd_Dmf_Using_Methanol_Dehydrogenation_Process_By_Mr_S._Srinivasan/user_defined_compound/Dimethylamine.json
new file mode 100644
index 0000000..4d4ad83
--- /dev/null
+++ b/Process_Development_For_The_Production_Of_100_Tpd_Dmf_Using_Methanol_Dehydrogenation_Process_By_Mr_S._Srinivasan/user_defined_compound/Dimethylamine.json
@@ -0,0 +1,204 @@
+{
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+  "BO_GOR": 0.0,
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+  "BO_OilViscTemp1": 0.0,
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+  "BO_PNA_N": 0.0,
+  "BO_PNA_P": 0.0,
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+  "CAS_Number": "124-40-3",
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+  "Chao_Seader_Liquid_Molar_Volume": 66.59,
+  "Chao_Seader_Solubility_Parameter": 9.18,
+  "Charge": 0,
+  "ChemicalStructure": "",
+  "Comments": "",
+  "CompCreatorStudyFile": "C:\\Users\\Srinivas\\Desktop\\Project_Files_2021\\Srinivasan-Project-works\\Dimethylamine.dwcsd2",
+  "COSMODBName": null,
+  "Critical_Compressibility": 0.27,
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+  "Electrolyte_DelHF": 0.0,
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+  "Ideal_Gas_Heat_Capacity_Const_D": 2.31E-05,
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+  "IG_Gibbs_Energy_of_Formation_25C": 1227.81721384206,
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+  "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": "4",
+  "LiquidHeatCapacityEquation": "0",
+  "LiquidThermalConductivityEquation": "0",
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+  "MolarVolume_v3i": 0.0,
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+  "NegativeIon": "",
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+  "Normal_Boiling_Point": 280.0,
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+  "PF_SG": null,
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+  "PF_Tv2": null,
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+  "PF_v2": null,
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+  "PF_vB": null,
+  "PF_Watson_K": null,
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+  "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": 164.96,
+  "Solid_Heat_Capacity_Tmin": 0.0,
+  "SolidDensityAtTs": 0.0,
+  "SolidDensityEquation": "2",
+  "SolidHeatCapacityEquation": "0",
+  "SolidTs": 0.0,
+  "SRK_Volume_Translation_Coefficient": 0.0,
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+  "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": 164.96,
+  "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": 0.27,
+  "Elements": {
+    "C": 2,
+    "H": 7,
+    "N": 1
+  },
+  "MODFACGroups": {
+    "1": "1",
+    "31": "1"
+  },
+  "NISTMODFACGroups": {
+    "1": "1",
+    "31": "1"
+  },
+  "UNIFACGroups": {
+    "1": "1",
+    "32": "1"
+  },
+  "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_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
deleted file mode 100644
index feab026..0000000
--- a/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/DWSIMFlowsheetAbstract.pdf
+++ /dev/null
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
deleted file mode 100644
index a16b4db..0000000
--- a/Production_Of_Acetaldehyde_By_Dehydrogenation_Of_Ethanol_Using_Activated_Carbon_As_Catalyst_By_Mr_Ananay_Mahajan/ProductionOfAcetaldehydeFlowsheet.dwxmz
+++ /dev/null
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
deleted file mode 100644
index 43c3708..0000000
--- a/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/Formaldehyde_Production.dwxmz
+++ /dev/null
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
deleted file mode 100644
index 41b65c6..0000000
--- a/Production_Of_Formaldehyde_By_Dehydrogenation_Of_Methanol_By_Mr_Karan_Saxena/formaldehyde_production.pdf
+++ /dev/null
diff --git a/Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Abstract_isobuteneProduction.pdf b/Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Abstract_isobuteneProduction.pdf
deleted file mode 100644
index 5405f28..0000000
--- a/Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Abstract_isobuteneProduction.pdf
+++ /dev/null
diff --git a/Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Flowsheet_isobuteneProduction.dwxml b/Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Flowsheet_isobuteneProduction.dwxml
deleted file mode 100644
index 1e9c0f1..0000000
--- a/Production_Of_Isobutene_From_Catalytic_Dehydrogenation_Of_Isobutane_By_Mr_Siddharth_Tiwari,_Sufiyan_Ahmed/Flowsheet_isobuteneProduction.dwxml
+++ /dev/null
@@ -1,13082 +0,0 @@
-<?xml version="1.0" encoding="utf-8"?>
-<DWSIM_Simulation_Data>
-  <GeneralInfo>
-    <BuildVersion>6.4.8.0</BuildVersion>
-    <BuildDate>2000-01-09T00:00:00</BuildDate>
-    <OSInfo>Microsoft Windows 7 Ultimate , Version 6.1.7601.65536, Win32NT Platform</OSInfo>
-    <SavedOn>2021-05-18T15:17:22.7902004+05:30</SavedOn>
-    <SavedFromClassicUI>true</SavedFromClassicUI>
-  </GeneralInfo>
-  <SimulationObjects>
-    <SimulationObject>
-      <Type>DWSIM.UnitOperations.UnitOperations.ComponentSeparator</Type>
-      <ObjectClass>Separators</ObjectClass>
-      <SpecifiedStreamIndex>0</SpecifiedStreamIndex>
-      <EnergyImb>1.07779159463917E-06</EnergyImb>
-      <MobileCompatible>true</MobileCompatible>
-      <ComponentDescription>ComponentSeparator</ComponentDescription>
-      <ComponentName>CS-ec247b58-c600-4da1-986c-504e0973a209</ComponentName>
-      <DynamicsSpec>Pressure</DynamicsSpec>
-      <DynamicsOnly>false</DynamicsOnly>
-      <Visible>true</Visible>
-      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
-      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
-      <Calculated>true</Calculated>
-      <DebugMode>false</DebugMode>
-      <LastUpdated>05/07/2021 15:28:35</LastUpdated>
-      <Annotation></Annotation>
-      <IsAdjustAttached>false</IsAdjustAttached>
-      <AttachedAdjustId></AttachedAdjustId>
-      <AdjustVarType>Manipulated</AdjustVarType>
-      <IsSpecAttached>false</IsSpecAttached>
-      <AttachedSpecId></AttachedSpecId>
-      <SpecVarType>Source</SpecVarType>
-      <Name>CS-ec247b58-c600-4da1-986c-504e0973a209</Name>
-      <SupportsDynamicMode>false</SupportsDynamicMode>
-      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
-      <DynamicProperties />
-      <DynamicPropertiesDescriptions />
-      <DynamicPropertiesUnitTypes />
-      <AttachedUtilities />
-      <PropertyPackage>PP-d1b661c9-196f-4d26-8584-e1d098c54cfc</PropertyPackage>
-      <SeparationSpecs>
-        <SeparationSpec ID="Isobutene" CompID="Isobutene" SepSpec="PercentInletMolarFlow" SpecUnit="%" SpecValue="0" />
-        <SeparationSpec ID="Isobutane" CompID="Isobutane" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="1" />
-        <SeparationSpec ID="Hydrogen" CompID="Hydrogen" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="0" />
-      </SeparationSpecs>
-    </SimulationObject>
-    <SimulationObject>
-      <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
-      <ObjectClass>Streams</ObjectClass>
-      <SupportsDynamicMode>true</SupportsDynamicMode>
-      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
-      <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
-      <AtEquilibrium>true</AtEquilibrium>
-      <ComponentDescription>CorrentedeMatria</ComponentDescription>
-      <ComponentName>MAT-4b7d43a7-e636-486c-8774-e32cb4995605</ComponentName>
-      <Name2>MAT-4b7d43a7-e636-486c-8774-e32cb4995605</Name2>
-      <code>0</code>
-      <InputComposition />
-      <IsElectrolyteStream>false</IsElectrolyteStream>
-      <ReferenceSolvent></ReferenceSolvent>
-      <SpecType>Temperature_and_Pressure</SpecType>
-      <CompositionBasis>Molar_Fractions</CompositionBasis>
-      <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
-      <MobileCompatible>true</MobileCompatible>
-      <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
-      <DefinedFlow>Mass</DefinedFlow>
-      <DynamicsSpec>Pressure</DynamicsSpec>
-      <DynamicsOnly>false</DynamicsOnly>
-      <Visible>true</Visible>
-      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
-      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
-      <Calculated>true</Calculated>
-      <DebugMode>false</DebugMode>
-      <LastUpdated>05/07/2021 15:30:39</LastUpdated>
-      <Annotation></Annotation>
-      <IsAdjustAttached>false</IsAdjustAttached>
-      <AttachedAdjustId></AttachedAdjustId>
-      <AdjustVarType>Manipulated</AdjustVarType>
-      <IsSpecAttached>false</IsSpecAttached>
-      <AttachedSpecId></AttachedSpecId>
-      <SpecVarType>Source</SpecVarType>
-      <Name>MAT-4b7d43a7-e636-486c-8774-e32cb4995605</Name>
-      <DynamicProperties />
-      <DynamicPropertiesDescriptions />
-      <DynamicPropertiesUnitTypes />
-      <AttachedUtilities />
-      <PropertyPackage>PP-d1b661c9-196f-4d26-8584-e1d098c54cfc</PropertyPackage>
-      <Phases>
-        <Phase>
-          <ID>0</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-            <thermalConductivity>0.090830372544599</thermalConductivity>
-            <volumetric_flow>0.474383163680183</volumetric_flow>
-            <gibbs_free_energy>-553.981235004842</gibbs_free_energy>
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-            <internal_energy>-116104.835645057</internal_energy>
-            <molar_gibbs_free_energy>-32198.6081371984</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>-6863316.16513183</molar_helmholtz_energy>
-            <molar_internal_energy>-6748268.47832912</molar_internal_energy>
-          </Properties>
-        </Phase>
-        <Phase>
-          <ID>1</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <ComponentName>Isobutene</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>0</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Isobutene</Name>
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-              <PartialVolume>8.15793244523351E-05</PartialVolume>
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-              <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
-              <EntropyF_Dmol>0</EntropyF_Dmol>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
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-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>0</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Isobutane</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>8.88395976096247E-05</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
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-              <EntropyF_Dmol>0</EntropyF_Dmol>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Hydrogen</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>2.55002235074774E-05</PartialVolume>
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-              <DynamicProperties />
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-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>OverallLiquid</ComponentName>
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-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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-            <density>NaN</density>
-            <enthalpy>0</enthalpy>
-            <entropy>0</entropy>
-            <heatCapacityCp>0</heatCapacityCp>
-            <heatCapacityCv>0</heatCapacityCv>
-            <kinematic_viscosity>NaN</kinematic_viscosity>
-            <massflow>0</massflow>
-            <massfraction>0</massfraction>
-            <molar_enthalpy>NaN</molar_enthalpy>
-            <molar_entropy>NaN</molar_entropy>
-            <molarflow>0</molarflow>
-            <molarfraction>0</molarfraction>
-            <molecularWeight>NaN</molecularWeight>
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-            <helmholtz_energy>0</helmholtz_energy>
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-            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
-            <molar_internal_energy>NaN</molar_internal_energy>
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-        <Phase>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
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-              <EntropyF_Dmol>0</EntropyF_Dmol>
-              <DynamicProperties />
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-            <Compound>
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-              <DynamicProperties />
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-            <Compound>
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-              <Name>Hydrogen</Name>
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-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
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-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Vapor</ComponentName>
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-        <Phase>
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-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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-        <PROP_MS_106_x002F_Isobutene>false</PROP_MS_106_x002F_Isobutene>
-        <PROP_MS_107_x002F_Isobutene>false</PROP_MS_107_x002F_Isobutene>
-        <PROP_MS_108_x002F_Isobutene>false</PROP_MS_108_x002F_Isobutene>
-        <PROP_MS_109_x002F_Isobutene>false</PROP_MS_109_x002F_Isobutene>
-        <PROP_MS_110_x002F_Isobutene>false</PROP_MS_110_x002F_Isobutene>
-        <PROP_MS_111_x002F_Isobutene>false</PROP_MS_111_x002F_Isobutene>
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-        <PROP_MS_113_x002F_Isobutene>false</PROP_MS_113_x002F_Isobutene>
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-        <PROP_MS_118_x002F_Isobutene>false</PROP_MS_118_x002F_Isobutene>
-        <PROP_MS_119_x002F_Isobutene>false</PROP_MS_119_x002F_Isobutene>
-        <PROP_MS_120_x002F_Isobutene>false</PROP_MS_120_x002F_Isobutene>
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-        <PROP_MS_102_x002F_Hydrogen>false</PROP_MS_102_x002F_Hydrogen>
-        <PROP_MS_103_x002F_Hydrogen>false</PROP_MS_103_x002F_Hydrogen>
-        <PROP_MS_104_x002F_Hydrogen>false</PROP_MS_104_x002F_Hydrogen>
-        <PROP_MS_105_x002F_Hydrogen>false</PROP_MS_105_x002F_Hydrogen>
-        <PROP_MS_106_x002F_Hydrogen>false</PROP_MS_106_x002F_Hydrogen>
-        <PROP_MS_107_x002F_Hydrogen>false</PROP_MS_107_x002F_Hydrogen>
-        <PROP_MS_108_x002F_Hydrogen>false</PROP_MS_108_x002F_Hydrogen>
-        <PROP_MS_109_x002F_Hydrogen>false</PROP_MS_109_x002F_Hydrogen>
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-        <PROP_MS_112_x002F_Hydrogen>false</PROP_MS_112_x002F_Hydrogen>
-        <PROP_MS_113_x002F_Hydrogen>false</PROP_MS_113_x002F_Hydrogen>
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-        <PROP_MS_233_x002F_Hydrogen>false</PROP_MS_233_x002F_Hydrogen>
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-        <PROP_MS_235_x002F_Hydrogen>false</PROP_MS_235_x002F_Hydrogen>
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-        <PROP_MS_239_x002F_Hydrogen>false</PROP_MS_239_x002F_Hydrogen>
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-        <PROP_MS_243_x002F_Hydrogen>false</PROP_MS_243_x002F_Hydrogen>
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-        <PROP_MS_245_x002F_Hydrogen>false</PROP_MS_245_x002F_Hydrogen>
-        <PROP_MS_154>false</PROP_MS_154>
-      </Properties>
-      <SortableItems>
-        <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>Custom</SortableItem>
-      </SortableItems>
-    </GraphicObject>
-  </GraphicObjects>
-  <PropertyPackages>
-    <PropertyPackage>
-      <ID>PP-d1b661c9-196f-4d26-8584-e1d098c54cfc</ID>
-      <Type>DWSIM.Thermodynamics.PropertyPackages.PengRobinsonPropertyPackage</Type>
-      <ComponentName>Peng-Robinson (PR)</ComponentName>
-      <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>
-      <TPSeverity>0</TPSeverity>
-      <TPCompIDs></TPCompIDs>
-      <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
-      <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
-      <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
-      <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
-      <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
-      <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
-      <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
-      <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
-      <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>
-      <EnthalpyEntropyCpCvCalculationMode>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
-      <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
-      <ActivityCoefficientModels_IgnoreMissingInteractionParameters>true</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
-      <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
-      <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
-      <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
-      <ForcedSolids>[]</ForcedSolids>
-      <PropertyOverrides>{}</PropertyOverrides>
-      <InteractionParameters>
-        <InteractionParameter Compound1="Hydrogen" Compound2="Isobutene" Value="0" />
-        <InteractionParameter Compound1="Isobutane" Compound2="Hydrogen" Value="0" />
-        <InteractionParameter Compound1="Isobutane" Compound2="Isobutene" Value="0" />
-      </InteractionParameters>
-      <FlashSettings>
-        <Setting Name="Replace_PTFlash" Value="False" />
-        <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" />
-        <Setting Name="PVFlash_MaximumTemperatureChange" Value="10" />
-        <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" />
-        <Setting Name="PTFlash_DampingFactor" Value="1" />
-        <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
-        <Setting Name="ImmiscibleWaterOption" Value="False" />
-        <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
-        <Setting Name="UseIOFlash" Value="False" />
-      </FlashSettings>
-    </PropertyPackage>
-  </PropertyPackages>
-  <Compounds>
-    <Compound>
-      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
-      <Acentric_Factor>0.2</Acentric_Factor>
-      <BO_BSW>0</BO_BSW>
-      <BO_GOR>0</BO_GOR>
-      <BO_OilVisc1>0</BO_OilVisc1>
-      <BO_OilVisc2>0</BO_OilVisc2>
-      <BO_OilViscTemp1>0</BO_OilViscTemp1>
-      <BO_OilViscTemp2>0</BO_OilViscTemp2>
-      <BO_PNA_A>0</BO_PNA_A>
-      <BO_PNA_N>0</BO_PNA_N>
-      <BO_PNA_P>0</BO_PNA_P>
-      <BO_SGG>0</BO_SGG>
-      <BO_SGO>0</BO_SGO>
-      <CAS_Number>115-11-7</CAS_Number>
-      <Chao_Seader_Acentricity>0.1951</Chao_Seader_Acentricity>
-      <Chao_Seader_Liquid_Molar_Volume>95.3727</Chao_Seader_Liquid_Molar_Volume>
-      <Chao_Seader_Solubility_Parameter>0.0032624691678</Chao_Seader_Solubility_Parameter>
-      <Charge>0</Charge>
-      <ChemicalStructure></ChemicalStructure>
-      <Comments></Comments>
-      <CompCreatorStudyFile></CompCreatorStudyFile>
-      <Critical_Compressibility>0.275</Critical_Compressibility>
-      <Critical_Pressure>4000000</Critical_Pressure>
-      <Critical_Temperature>417.9</Critical_Temperature>
-      <Critical_Volume>0.2388</Critical_Volume>
-      <CurrentDB>ChemSep</CurrentDB>
-      <Dipole_Moment>1.67E-30</Dipole_Moment>
-      <Electrolyte_Cp0>0</Electrolyte_Cp0>
-      <Electrolyte_DelGF>0</Electrolyte_DelGF>
-      <Electrolyte_DelHF>0</Electrolyte_DelHF>
-      <EnthalpyOfFusionAtTf>5.9312</EnthalpyOfFusionAtTf>
-      <Formula>CH2C(CH3)2</Formula>
-      <HVap_A>39160000</HVap_A>
-      <HVap_B>1.1638</HVap_B>
-      <HVap_C>-1.4033</HVap_C>
-      <HVap_D>0.81203</HVap_D>
-      <HVap_E>-0.13521</HVap_E>
-      <HVap_TMAX>417.9</HVap_TMAX>
-      <HVap_TMIN>132.81</HVap_TMIN>
-      <HydrationNumber>0</HydrationNumber>
-      <ID>207</ID>
-      <Ideal_Gas_Heat_Capacity_Const_A>49784</Ideal_Gas_Heat_Capacity_Const_A>
-      <Ideal_Gas_Heat_Capacity_Const_B>-472.84</Ideal_Gas_Heat_Capacity_Const_B>
-      <Ideal_Gas_Heat_Capacity_Const_C>12.012</Ideal_Gas_Heat_Capacity_Const_C>
-      <Ideal_Gas_Heat_Capacity_Const_D>0.00052863</Ideal_Gas_Heat_Capacity_Const_D>
-      <Ideal_Gas_Heat_Capacity_Const_E>-1.7772E-07</Ideal_Gas_Heat_Capacity_Const_E>
-      <IdealgasCpEquation>16</IdealgasCpEquation>
-      <IG_Enthalpy_of_Formation_25C>-304.778499106696</IG_Enthalpy_of_Formation_25C>
-      <IG_Entropy_of_Formation_25C>-4.49423443846045</IG_Entropy_of_Formation_25C>
-      <IG_Gibbs_Energy_of_Formation_25C>1035.17749872029</IG_Gibbs_Energy_of_Formation_25C>
-      <InChI></InChI>
-      <Ion_CpAq_a>0</Ion_CpAq_a>
-      <Ion_CpAq_b>0</Ion_CpAq_b>
-      <Ion_CpAq_c>0</Ion_CpAq_c>
-      <IsBlackOil>false</IsBlackOil>
-      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
-      <IsFPROPSSupported>false</IsFPROPSSupported>
-      <IsHydratedSalt>false</IsHydratedSalt>
-      <IsHYPO>0</IsHYPO>
-      <IsIon>false</IsIon>
-      <IsModified>false</IsModified>
-      <IsPF>0</IsPF>
-      <IsSalt>false</IsSalt>
-      <Liquid_Density_Const_A>1.01</Liquid_Density_Const_A>
-      <Liquid_Density_Const_B>0.25611</Liquid_Density_Const_B>
-      <Liquid_Density_Const_C>417.9</Liquid_Density_Const_C>
-      <Liquid_Density_Const_D>0.2642</Liquid_Density_Const_D>
-      <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
-      <Liquid_Density_Tmax>417.9</Liquid_Density_Tmax>
-      <Liquid_Density_Tmin>132.81</Liquid_Density_Tmin>
-      <Liquid_Heat_Capacity_Const_A>95317</Liquid_Heat_Capacity_Const_A>
-      <Liquid_Heat_Capacity_Const_B>-68.58</Liquid_Heat_Capacity_Const_B>
-      <Liquid_Heat_Capacity_Const_C>9.3268</Liquid_Heat_Capacity_Const_C>
-      <Liquid_Heat_Capacity_Const_D>0.0023434</Liquid_Heat_Capacity_Const_D>
-      <Liquid_Heat_Capacity_Const_E>7.6824E-06</Liquid_Heat_Capacity_Const_E>
-      <Liquid_Heat_Capacity_Tmax>343.15</Liquid_Heat_Capacity_Tmax>
-      <Liquid_Heat_Capacity_Tmin>132.81</Liquid_Heat_Capacity_Tmin>
-      <Liquid_Thermal_Conductivity_Const_A>0.061493</Liquid_Thermal_Conductivity_Const_A>
-      <Liquid_Thermal_Conductivity_Const_B>33.335</Liquid_Thermal_Conductivity_Const_B>
-      <Liquid_Thermal_Conductivity_Const_C>-2.4686</Liquid_Thermal_Conductivity_Const_C>
-      <Liquid_Thermal_Conductivity_Const_D>0.0041425</Liquid_Thermal_Conductivity_Const_D>
-      <Liquid_Thermal_Conductivity_Const_E>-2.3609E-05</Liquid_Thermal_Conductivity_Const_E>
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-      <Liquid_Viscosity_Const_A>-12.717</Liquid_Viscosity_Const_A>
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-      <Liquid_Viscosity_Const_D>-2.3983E-06</Liquid_Viscosity_Const_D>
-      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
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-      <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
-      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
-      <LiquidViscosityEquation>101</LiquidViscosityEquation>
-      <Molar_Weight>56.10632</Molar_Weight>
-      <MolarVolume_k1i>0</MolarVolume_k1i>
-      <MolarVolume_k2i>0</MolarVolume_k2i>
-      <MolarVolume_k3i>0</MolarVolume_k3i>
-      <MolarVolume_v2i>0</MolarVolume_v2i>
-      <MolarVolume_v3i>0</MolarVolume_v3i>
-      <Name>Isobutene</Name>
-      <NegativeIon></NegativeIon>
-      <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
-      <Normal_Boiling_Point>266.24</Normal_Boiling_Point>
-      <OriginalDB>ChemSep</OriginalDB>
-      <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
-      <PC_SAFT_m>0</PC_SAFT_m>
-      <PC_SAFT_sigma>0</PC_SAFT_sigma>
-      <PositiveIon></PositiveIon>
-      <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
-      <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
-      <SMILES>C=C(C)C</SMILES>
-      <Solid_Density_Const_A>17.138</Solid_Density_Const_A>
-      <Solid_Density_Const_B>-0.014341</Solid_Density_Const_B>
-      <Solid_Density_Const_C>0</Solid_Density_Const_C>
-      <Solid_Density_Const_D>0</Solid_Density_Const_D>
-      <Solid_Density_Const_E>0</Solid_Density_Const_E>
-      <Solid_Density_Tmax>132.81</Solid_Density_Tmax>
-      <Solid_Density_Tmin>53.12</Solid_Density_Tmin>
-      <Solid_Heat_Capacity_Const_A>34336</Solid_Heat_Capacity_Const_A>
-      <Solid_Heat_Capacity_Const_B>57.654</Solid_Heat_Capacity_Const_B>
-      <Solid_Heat_Capacity_Const_C>2.3469</Solid_Heat_Capacity_Const_C>
-      <Solid_Heat_Capacity_Const_D>-0.0024921</Solid_Heat_Capacity_Const_D>
-      <Solid_Heat_Capacity_Const_E>7.6414E-06</Solid_Heat_Capacity_Const_E>
-      <Solid_Heat_Capacity_Tmax>130</Solid_Heat_Capacity_Tmax>
-      <Solid_Heat_Capacity_Tmin>80</Solid_Heat_Capacity_Tmin>
-      <SolidDensityAtTs>0</SolidDensityAtTs>
-      <SolidDensityEquation>2</SolidDensityEquation>
-      <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
-      <SolidTs>0</SolidTs>
-      <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
-      <StandardStateMolarVolume>0</StandardStateMolarVolume>
-      <StoichSum>0</StoichSum>
-      <Surface_Tension_Const_A>-0.0085717</Surface_Tension_Const_A>
-      <Surface_Tension_Const_B>38.109</Surface_Tension_Const_B>
-      <Surface_Tension_Const_C>-3.4301</Surface_Tension_Const_C>
-      <Surface_Tension_Const_D>0.0015866</Surface_Tension_Const_D>
-      <Surface_Tension_Const_E>-1.2058E-05</Surface_Tension_Const_E>
-      <Surface_Tension_Tmax>417.9</Surface_Tension_Tmax>
-      <Surface_Tension_Tmin>132.81</Surface_Tension_Tmin>
-      <SurfaceTensionEquation>16</SurfaceTensionEquation>
-      <TemperatureOfFusion>132.81</TemperatureOfFusion>
-      <UNIQUAC_Q>2.684</UNIQUAC_Q>
-      <UNIQUAC_R>2.9195</UNIQUAC_R>
-      <Vapor_Pressure_Constant_A>47.13879</Vapor_Pressure_Constant_A>
-      <Vapor_Pressure_Constant_B>-3682.162</Vapor_Pressure_Constant_B>
-      <Vapor_Pressure_Constant_C>-3.952514</Vapor_Pressure_Constant_C>
-      <Vapor_Pressure_Constant_D>4.044185E-06</Vapor_Pressure_Constant_D>
-      <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
-      <Vapor_Pressure_TMAX>417.9</Vapor_Pressure_TMAX>
-      <Vapor_Pressure_TMIN>132.81</Vapor_Pressure_TMIN>
-      <Vapor_Thermal_Conductivity_Const_A>-418.21</Vapor_Thermal_Conductivity_Const_A>
-      <Vapor_Thermal_Conductivity_Const_B>0.91306</Vapor_Thermal_Conductivity_Const_B>
-      <Vapor_Thermal_Conductivity_Const_C>-1510500000</Vapor_Thermal_Conductivity_Const_C>
-      <Vapor_Thermal_Conductivity_Const_D>31789000000</Vapor_Thermal_Conductivity_Const_D>
-      <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
-      <Vapor_Thermal_Conductivity_Tmax>1000</Vapor_Thermal_Conductivity_Tmax>
-      <Vapor_Thermal_Conductivity_Tmin>132.81</Vapor_Thermal_Conductivity_Tmin>
-      <Vapor_Viscosity_Const_A>2.8839E-06</Vapor_Viscosity_Const_A>
-      <Vapor_Viscosity_Const_B>0.33897</Vapor_Viscosity_Const_B>
-      <Vapor_Viscosity_Const_C>365.04</Vapor_Viscosity_Const_C>
-      <Vapor_Viscosity_Const_D>17752</Vapor_Viscosity_Const_D>
-      <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
-      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
-      <Vapor_Viscosity_Tmin>132.81</Vapor_Viscosity_Tmin>
-      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
-      <VaporPressureEquation>101</VaporPressureEquation>
-      <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
-      <VaporViscosityEquation>102</VaporViscosityEquation>
-      <Z_Rackett>0.2727</Z_Rackett>
-      <FullerDiffusionVolume>82.08</FullerDiffusionVolume>
-      <LennardJonesDiameter>5.449925E-10</LennardJonesDiameter>
-      <LennardJonesEnergy>261.5672</LennardJonesEnergy>
-      <Parachor>0.0318</Parachor>
-      <Tag></Tag>
-      <DynamicProperties />
-      <UNIFACGroups>
-        <Item GroupID="1" Value="2" />
-        <Item GroupID="7" Value="1" />
-      </UNIFACGroups>
-      <MODFACGroups>
-        <Item GroupID="1" Value="2" />
-        <Item GroupID="7" Value="1" />
-      </MODFACGroups>
-      <NISTMODFACGroups>
-        <Item GroupID="1" Value="2" />
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-      </NISTMODFACGroups>
-      <Elements>
-        <Item Name="C" Value="4" />
-        <Item Name="H" Value="8" />
-      </Elements>
-    </Compound>
-    <Compound>
-      <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
-      <Acentric_Factor>0.186</Acentric_Factor>
-      <BO_BSW>0</BO_BSW>
-      <BO_GOR>0</BO_GOR>
-      <BO_OilVisc1>0</BO_OilVisc1>
-      <BO_OilVisc2>0</BO_OilVisc2>
-      <BO_OilViscTemp1>0</BO_OilViscTemp1>
-      <BO_OilViscTemp2>0</BO_OilViscTemp2>
-      <BO_PNA_A>0</BO_PNA_A>
-      <BO_PNA_N>0</BO_PNA_N>
-      <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>
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-      <Ideal_Gas_Heat_Capacity_Const_C>12.02593</Ideal_Gas_Heat_Capacity_Const_C>
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-      <Ideal_Gas_Heat_Capacity_Const_E>-2.59608E-07</Ideal_Gas_Heat_Capacity_Const_E>
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-      <IG_Enthalpy_of_Formation_25C>-2322.52048270712</IG_Enthalpy_of_Formation_25C>
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-      <InChI></InChI>
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-      <IsBlackOil>false</IsBlackOil>
-      <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
-      <IsFPROPSSupported>false</IsFPROPSSupported>
-      <IsHydratedSalt>false</IsHydratedSalt>
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-      <IsIon>false</IsIon>
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-      <IsPF>0</IsPF>
-      <IsSalt>false</IsSalt>
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-      <Liquid_Density_Tmin>113.54</Liquid_Density_Tmin>
-      <Liquid_Heat_Capacity_Const_A>89466</Liquid_Heat_Capacity_Const_A>
-      <Liquid_Heat_Capacity_Const_B>-323.61</Liquid_Heat_Capacity_Const_B>
-      <Liquid_Heat_Capacity_Const_C>12.827</Liquid_Heat_Capacity_Const_C>
-      <Liquid_Heat_Capacity_Const_D>-0.010476</Liquid_Heat_Capacity_Const_D>
-      <Liquid_Heat_Capacity_Const_E>2.5037E-05</Liquid_Heat_Capacity_Const_E>
-      <Liquid_Heat_Capacity_Tmax>380</Liquid_Heat_Capacity_Tmax>
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-      <Liquid_Thermal_Conductivity_Const_A>0.029586</Liquid_Thermal_Conductivity_Const_A>
-      <Liquid_Thermal_Conductivity_Const_B>56.323</Liquid_Thermal_Conductivity_Const_B>
-      <Liquid_Thermal_Conductivity_Const_C>-2.8746</Liquid_Thermal_Conductivity_Const_C>
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-      <Liquid_Thermal_Conductivity_Const_E>-1.7826E-05</Liquid_Thermal_Conductivity_Const_E>
-      <Liquid_Thermal_Conductivity_Tmax>400</Liquid_Thermal_Conductivity_Tmax>
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-      <Liquid_Viscosity_Const_A>-39.10125</Liquid_Viscosity_Const_A>
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-      <Liquid_Viscosity_Const_C>4.876982</Liquid_Viscosity_Const_C>
-      <Liquid_Viscosity_Const_D>-2.03993E-05</Liquid_Viscosity_Const_D>
-      <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
-      <LiquidDensityEquation>105</LiquidDensityEquation>
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-      <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
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-      <Molar_Weight>58.1222</Molar_Weight>
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-      <MolarVolume_v3i>0</MolarVolume_v3i>
-      <Name>Isobutane</Name>
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-      <Normal_Boiling_Point>261.34</Normal_Boiling_Point>
-      <OriginalDB>ChemSep</OriginalDB>
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-      <SMILES>CC(C)C</SMILES>
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-      <Vapor_Viscosity_Const_A>3.951E-08</Vapor_Viscosity_Const_A>
-      <Vapor_Viscosity_Const_B>0.90975</Vapor_Viscosity_Const_B>
-      <Vapor_Viscosity_Const_C>-52.076</Vapor_Viscosity_Const_C>
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-      <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
-      <Vapor_Viscosity_Tmin>150</Vapor_Viscosity_Tmin>
-      <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
-      <VaporPressureEquation>101</VaporPressureEquation>
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-      <VaporViscosityEquation>102</VaporViscosityEquation>
-      <Z_Rackett>0.275</Z_Rackett>
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-      <Tag></Tag>
-      <DynamicProperties />
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-      <CurrentDB>ChemSep</CurrentDB>
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-      <EnthalpyOfFusionAtTf>0.1171</EnthalpyOfFusionAtTf>
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-      <Ideal_Gas_Heat_Capacity_Const_C>10.36209</Ideal_Gas_Heat_Capacity_Const_C>
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-      <Molar_Weight>2.01588</Molar_Weight>
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-      <Name>Hydrogen</Name>
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-      <SMILES>[H][H]</SMILES>
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-      <Solid_Heat_Capacity_Const_B>-1.3847E-11</Solid_Heat_Capacity_Const_B>
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-      <Solid_Heat_Capacity_Const_D>-1.2321E-13</Solid_Heat_Capacity_Const_D>
-      <Solid_Heat_Capacity_Const_E>4.114E-15</Solid_Heat_Capacity_Const_E>
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-      <Description>Default Reaction Set</Description>
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-      <Type>DWSIM.Thermodynamics.BaseClasses.Reaction</Type>
-      <BaseReactant>Isobutene</BaseReactant>
-      <Description></Description>
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-      <Name>isobutene rxn</Name>
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-      <ReactionPhase>Vapor</ReactionPhase>
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-      <A_Forward>13.99</A_Forward>
-      <A_Reverse>12.42</A_Reverse>
-      <Approach>0</Approach>
-      <ConcUnit>bar</ConcUnit>
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-      <E_Forward>112000</E_Forward>
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-      <Expression></Expression>
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-      <RateEquationNumerator></RateEquationNumerator>
-      <ReactionGibbsEnergy>79520.0000000002</ReactionGibbsEnergy>
-      <Tmax>2000</Tmax>
-      <Tmin>0</Tmin>
-      <VelUnit>mol/[m3.s]</VelUnit>
-      <ReactionKinFwdType>Arrhenius</ReactionKinFwdType>
-      <ReactionKinRevType>Arrhenius</ReactionKinRevType>
-      <ReactionKinFwdExpression></ReactionKinFwdExpression>
-      <ReactionKinRevExpression></ReactionKinRevExpression>
-      <E_Forward_Unit>J/mol</E_Forward_Unit>
-      <E_Reverse_Unit>J/mol</E_Reverse_Unit>
-      <ReactionKinetics>Expression</ReactionKinetics>
-      <ScriptTitle></ScriptTitle>
-      <EquilibriumReactionBasisUnits>Pa</EquilibriumReactionBasisUnits>
-      <Compounds>
-        <Compound Name="Isobutene" StoichCoeff="1" DirectOrder="1" ReverseOrder="-1" IsBaseReactant="true" />
-        <Compound Name="Isobutane" StoichCoeff="-1" DirectOrder="-1" ReverseOrder="1" IsBaseReactant="false" />
-        <Compound Name="Hydrogen" StoichCoeff="1" DirectOrder="1" ReverseOrder="-1" IsBaseReactant="false" />
-      </Compounds>
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-    <Description></Description>
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-    <EventSetList />
-    <IntegratorList />
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-  <OptimizationCases />
-  <SensitivityAnalysis />
-  <PetroleumAssays />
-  <WatchItems />
-  <ScriptItems />
-  <ChartItems />
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diff --git a/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/Abstract.pdf b/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/Abstract.pdf
deleted file mode 100644
index 38b6585..0000000
--- a/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/Abstract.pdf
+++ /dev/null
diff --git a/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/DC_with_table.dwxmz b/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/DC_with_table.dwxmz
deleted file mode 100644
index be7cf3e..0000000
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+++ /dev/null
diff --git a/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/user_defined_compound/Methyl_DiEthanolAmine.zip b/Production_Of_Methyl_Diethanolamine_Using_Methylamine_And_Ethylene_Oxide_By_Ms_Gayathri_R_And_Aarthi_G/user_defined_compound/Methyl_DiEthanolAmine.zip
deleted file mode 100644
index daa8237..0000000
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diff --git a/Production_Of_Terepthalic_Acid_From_Oxidation_Of_P-Xylene_By_Mr_Kaushal_Sannjay_Yadav,_Ms_Riyaben_Yogeshbhai_Tailor_&_Nikunj_Shantilal_Prajapati/finalabstract.pdf b/Production_Of_Terepthalic_Acid_From_Oxidation_Of_P-Xylene_By_Mr_Kaushal_Sannjay_Yadav,_Ms_Riyaben_Yogeshbhai_Tailor_&_Nikunj_Shantilal_Prajapati/finalabstract.pdf
deleted file mode 100644
index af0d7fe..0000000
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+++ /dev/null
diff --git a/Production_Of_Terepthalic_Acid_From_Oxidation_Of_P-Xylene_By_Mr_Kaushal_Sannjay_Yadav,_Ms_Riyaben_Yogeshbhai_Tailor_&_Nikunj_Shantilal_Prajapati/finalrun.dwxml b/Production_Of_Terepthalic_Acid_From_Oxidation_Of_P-Xylene_By_Mr_Kaushal_Sannjay_Yadav,_Ms_Riyaben_Yogeshbhai_Tailor_&_Nikunj_Shantilal_Prajapati/finalrun.dwxml
deleted file mode 100644
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-              <MolarFlow>0</MolarFlow>
-              <Name>Acetic acid</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>P-xylene</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>P-xylene</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Terephthalic acid</ComponentName>
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-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>Terephthalic acid</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>Water</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Solid</ComponentName>
-          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
-          <Name>Solid</Name>
-          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
-            <gibbs_free_energy>0</gibbs_free_energy>
-            <helmholtz_energy>0</helmholtz_energy>
-            <internal_energy>0</internal_energy>
-            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>0</molar_helmholtz_energy>
-            <molar_internal_energy>0</molar_internal_energy>
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-        </Phase>
-      </Phases>
-    </SimulationObject>
-    <SimulationObject>
-      <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
-      <ObjectClass>Streams</ObjectClass>
-      <SupportsDynamicMode>true</SupportsDynamicMode>
-      <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
-      <ComponentDescription>CorrentedeEnergia</ComponentDescription>
-      <ComponentName>EN-3df52840-6b3b-48c4-b702-06e63fbd4004</ComponentName>
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-      <DynamicsSpec>Pressure</DynamicsSpec>
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-      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
-      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
-      <Calculated>true</Calculated>
-      <DebugMode>false</DebugMode>
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-      <AttachedAdjustId></AttachedAdjustId>
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-      <DynamicPropertiesDescriptions />
-      <DynamicPropertiesUnitTypes />
-      <AttachedUtilities />
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-    <SimulationObject>
-      <Type>DWSIM.UnitOperations.UnitOperations.SolidsSeparator</Type>
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-      <ComponentDescription>SolidsSeparator</ComponentDescription>
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-      <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
-      <Calculated>true</Calculated>
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-      <DynamicProperties />
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-      <DynamicPropertiesUnitTypes />
-      <AttachedUtilities />
-      <PropertyPackage></PropertyPackage>
-    </SimulationObject>
-    <SimulationObject>
-      <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
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-      <code>0</code>
-      <InputComposition />
-      <IsElectrolyteStream>false</IsElectrolyteStream>
-      <ReferenceSolvent></ReferenceSolvent>
-      <SpecType>Pressure_and_Enthalpy</SpecType>
-      <CompositionBasis>Molar_Fractions</CompositionBasis>
-      <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
-      <MobileCompatible>true</MobileCompatible>
-      <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
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-      <DynamicsOnly>false</DynamicsOnly>
-      <Visible>true</Visible>
-      <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
-      <PreferredFlashAlgorithmTag>Nested Loops (VLE)</PreferredFlashAlgorithmTag>
-      <Calculated>true</Calculated>
-      <DebugMode>false</DebugMode>
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-      <IsAdjustAttached>false</IsAdjustAttached>
-      <AttachedAdjustId></AttachedAdjustId>
-      <AdjustVarType>Manipulated</AdjustVarType>
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-      <DynamicPropertiesUnitTypes />
-      <AttachedUtilities />
-      <PropertyPackage>PP-937e5791-4595-474e-9731-db2af504d882</PropertyPackage>
-      <Phases>
-        <Phase>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <Kvalue>NaN</Kvalue>
-              <lnKvalue>NaN</lnKvalue>
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-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <MassFraction>0.245792467875344</MassFraction>
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-              <FugacityCoeff>0</FugacityCoeff>
-              <Kvalue>NaN</Kvalue>
-              <lnKvalue>NaN</lnKvalue>
-              <MassFlow>0.70639464824313</MassFlow>
-              <MolarFlow>11.7630573297379</MolarFlow>
-              <Name>Acetic acid</Name>
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-              <VolumetricFlow>0.16432997120352</VolumetricFlow>
-              <VolumetricFraction>0.485727683967392</VolumetricFraction>
-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <MassFraction>0.0495289865238618</MassFraction>
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-              <FugacityCoeff>0</FugacityCoeff>
-              <Kvalue>NaN</Kvalue>
-              <lnKvalue>NaN</lnKvalue>
-              <MassFlow>0.142343706932086</MassFlow>
-              <MolarFlow>1.34077809948746</MolarFlow>
-              <Name>P-xylene</Name>
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-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Terephthalic acid</ComponentName>
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-              <MassFraction>0.703788716758689</MassFraction>
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-              <Kvalue>NaN</Kvalue>
-              <lnKvalue>NaN</lnKvalue>
-              <MassFlow>2.02265182212327</MassFlow>
-              <MolarFlow>12.1750561733481</MolarFlow>
-              <Name>Terephthalic acid</Name>
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-              <VolumetricFlow>0.1544874535374</VolumetricFlow>
-              <VolumetricFraction>0.456635101066298</VolumetricFraction>
-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <MoleFraction>3.55358087754847E-17</MoleFraction>
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-              <Molality>0</Molality>
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-              <Kvalue>NaN</Kvalue>
-              <lnKvalue>NaN</lnKvalue>
-              <MassFlow>1.62343948923615E-17</MassFlow>
-              <MolarFlow>9.01145854650134E-16</MolarFlow>
-              <Name>Water</Name>
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-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
-              <DynamicProperties />
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-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
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-          <Properties>
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-            <molecularWeight>113.331319471358</molecularWeight>
-            <pressure>434658.333333333</pressure>
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-            <temperature>731.801219994167</temperature>
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-              <MassFraction>NaN</MassFraction>
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-              <Molarity>0</Molarity>
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-              <FugacityCoeff>NaN</FugacityCoeff>
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-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
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-              <PartialVolume>2.69052034313602E-05</PartialVolume>
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-            <Compound>
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-              <PetroleumFraction>false</PetroleumFraction>
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-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Acetic acid</Name>
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-              <PartialVolume>6.85349494626964E-05</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <ComponentName>P-xylene</ComponentName>
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-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
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-              <lnKvalue>0</lnKvalue>
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-              <MolarFlow>NaN</MolarFlow>
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-              <DynamicProperties />
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-            <Compound>
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-              <ComponentName>Terephthalic acid</ComponentName>
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-              <Molarity>0</Molarity>
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-              <Kvalue>0</Kvalue>
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-              <MolarFlow>NaN</MolarFlow>
-              <Name>Terephthalic acid</Name>
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-              <PartialVolume>0.000168128168666</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
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-              <Molarity>0</Molarity>
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-              <MolarFlow>NaN</MolarFlow>
-              <Name>Water</Name>
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-              <PartialVolume>1.73065043772808E-05</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>OverallLiquid</ComponentName>
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-          <Name>OverallLiquid</Name>
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-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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-            <density>NaN</density>
-            <enthalpy>0</enthalpy>
-            <entropy>0</entropy>
-            <heatCapacityCp>0</heatCapacityCp>
-            <heatCapacityCv>0</heatCapacityCv>
-            <kinematic_viscosity>NaN</kinematic_viscosity>
-            <massflow>0</massflow>
-            <massfraction>0</massfraction>
-            <molar_enthalpy>NaN</molar_enthalpy>
-            <molar_entropy>NaN</molar_entropy>
-            <molarflow>0</molarflow>
-            <molarfraction>0</molarfraction>
-            <molecularWeight>NaN</molecularWeight>
-            <thermalConductivity>0</thermalConductivity>
-            <viscosity>0</viscosity>
-            <volumetric_flow>0</volumetric_flow>
-            <gibbs_free_energy>0</gibbs_free_energy>
-            <helmholtz_energy>0</helmholtz_energy>
-            <internal_energy>0</internal_energy>
-            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
-            <molar_internal_energy>NaN</molar_internal_energy>
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-        <Phase>
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-            <Compound>
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-            <heatCapacityCp>0.997155920436547</heatCapacityCp>
-            <heatCapacityCv>0.734471086183308</heatCapacityCv>
-            <massflow>4.44427777777778</massflow>
-            <molar_enthalpy>8377.08039318116</molar_enthalpy>
-            <molar_entropy>-0.0254213282436062</molar_entropy>
-            <molarflow>138.888888888889</molarflow>
-            <molecularWeight>31.9988</molecularWeight>
-            <pressure>1101325</pressure>
-            <surfaceTension>NaN</surfaceTension>
-            <temperature>573.560955169617</temperature>
-            <thermalConductivity>0.0466645854863644</thermalConductivity>
-            <volumetric_flow>0.602463644101145</volumetric_flow>
-            <gibbs_free_energy>262.24924292443</gibbs_free_energy>
-            <helmholtz_energy>-149032.710707005</helmholtz_energy>
-            <internal_energy>-149033.166370383</internal_energy>
-            <molar_gibbs_free_energy>8391.66107449024</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>-4768867.9033713</molar_helmholtz_energy>
-            <molar_internal_energy>-4768882.48405261</molar_internal_energy>
-          </Properties>
-        </Phase>
-        <Phase>
-          <ID>1</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Oxygen</ComponentName>
-              <ActivityCoeff>NaN</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Oxygen</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>2.69052034313602E-05</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Acetic acid</ComponentName>
-              <ActivityCoeff>NaN</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Acetic acid</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>0.000144477349338372</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>P-xylene</ComponentName>
-              <ActivityCoeff>NaN</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>P-xylene</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>0.00020598762446708</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Terephthalic acid</ComponentName>
-              <ActivityCoeff>NaN</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Terephthalic acid</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>0.000143269703085826</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Water</ComponentName>
-              <ActivityCoeff>NaN</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>NaN</MassFraction>
-              <MoleFraction>NaN</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>NaN</MassFlow>
-              <MolarFlow>NaN</MolarFlow>
-              <Name>Water</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>2.64719896316975E-05</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>OverallLiquid</ComponentName>
-          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
-          <Name>OverallLiquid</Name>
-          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
-            <compressibilityFactor>0</compressibilityFactor>
-            <density>NaN</density>
-            <enthalpy>0</enthalpy>
-            <entropy>0</entropy>
-            <heatCapacityCp>0</heatCapacityCp>
-            <heatCapacityCv>0</heatCapacityCv>
-            <kinematic_viscosity>NaN</kinematic_viscosity>
-            <massflow>0</massflow>
-            <massfraction>0</massfraction>
-            <molar_enthalpy>NaN</molar_enthalpy>
-            <molar_entropy>NaN</molar_entropy>
-            <molarflow>0</molarflow>
-            <molarfraction>0</molarfraction>
-            <molecularWeight>NaN</molecularWeight>
-            <thermalConductivity>0</thermalConductivity>
-            <viscosity>0</viscosity>
-            <volumetric_flow>0</volumetric_flow>
-            <gibbs_free_energy>0</gibbs_free_energy>
-            <helmholtz_energy>0</helmholtz_energy>
-            <internal_energy>0</internal_energy>
-            <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
-            <molar_internal_energy>NaN</molar_internal_energy>
-          </Properties>
-        </Phase>
-        <Phase>
-          <ID>2</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Oxygen</ComponentName>
-              <ActivityCoeff>5.76721425733662E-08</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>1</MassFraction>
-              <MoleFraction>1</MoleFraction>
-              <Molarity>230.534888285428</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>1.00179910405592</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>4.44427777777778</MassFlow>
-              <MolarFlow>138.888888888889</MolarFlow>
-              <Name>Oxygen</Name>
-              <PartialPressure>1101325</PartialPressure>
-              <PartialVolume>4.33773876064918</PartialVolume>
-              <VolumetricFlow>0.602463644101145</VolumetricFlow>
-              <VolumetricFraction>1</VolumetricFraction>
-              <DiffusionCoefficient>2.83436251542549E-11</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Acetic acid</ComponentName>
-              <ActivityCoeff>0.251482056564823</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>0.985545720668015</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>Acetic acid</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>P-xylene</ComponentName>
-              <ActivityCoeff>0.532316305778104</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>0.985156424649229</FugacityCoeff>
-              <Kvalue>0</Kvalue>
-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>P-xylene</Name>
-              <PartialPressure>0</PartialPressure>
-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Terephthalic acid</ComponentName>
-              <ActivityCoeff>29596.4785840087</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
-              <Molality>0</Molality>
-              <FugacityCoeff>0.954482123625887</FugacityCoeff>
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-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>Terephthalic acid</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
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-              <FugacityCoeff>0.988385537351245</FugacityCoeff>
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-              <MolarFlow>0</MolarFlow>
-              <Name>Water</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Vapor</ComponentName>
-          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
-          <Name>Vapor</Name>
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-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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-            <heatCapacityCp>0.997155920436547</heatCapacityCp>
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-            <jouleThomsonCoefficient>7.49285037365623E-06</jouleThomsonCoefficient>
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-            <massflow>4.44427777777778</massflow>
-            <massfraction>1</massfraction>
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-            <molar_entropy>-0.0254213282436062</molar_entropy>
-            <molarflow>138.888888888889</molarflow>
-            <molarfraction>1</molarfraction>
-            <molecularWeight>31.9988</molecularWeight>
-            <speedOfSound>NaN</speedOfSound>
-            <thermalConductivity>0.0466645854863644</thermalConductivity>
-            <viscosity>3.39004327227597E-05</viscosity>
-            <volumetric_flow>0.602463644101145</volumetric_flow>
-            <bulk_modulus>-306141200.899413</bulk_modulus>
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-            <helmholtz_energy>-149032.710707005</helmholtz_energy>
-            <internal_energy>-149033.166370383</internal_energy>
-            <isothermal_compressibility>-3.26646657510357E-09</isothermal_compressibility>
-            <molar_gibbs_free_energy>8391.66107449024</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>-4768867.9033713</molar_helmholtz_energy>
-            <molar_internal_energy>-4768882.48405261</molar_internal_energy>
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-        </Phase>
-        <Phase>
-          <ID>3</ID>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
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-              <PetroleumFraction>false</PetroleumFraction>
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-              <lnKvalue>0</lnKvalue>
-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>Oxygen</Name>
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-              <PartialVolume>0</PartialVolume>
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-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>Infinity</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <lnKvalue>0</lnKvalue>
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-              <Name>Acetic acid</Name>
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-              <PartialVolume>0</PartialVolume>
-              <VolumetricFlow>0</VolumetricFlow>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <ComponentName>P-xylene</ComponentName>
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-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>P-xylene</Name>
-              <PartialPressure>1101325</PartialPressure>
-              <PartialVolume>0</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
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-              <ComponentName>Terephthalic acid</ComponentName>
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-              <PetroleumFraction>false</PetroleumFraction>
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-              <Name>Terephthalic acid</Name>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
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-              <Name>Water</Name>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
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-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Liquid1</ComponentName>
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-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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-            <internal_energy>0</internal_energy>
-            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
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-        <Phase>
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-              <Name>Oxygen</Name>
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-              <PartialVolume>2.69052034313602E-05</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
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-              <ComponentName>Acetic acid</ComponentName>
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-              <MolarFlow>0</MolarFlow>
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-              <Name>Acetic acid</Name>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
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-              <Name>P-xylene</Name>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <DynamicProperties />
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-              <FugacityCoeff>NaN</FugacityCoeff>
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-              <MassFlow>0</MassFlow>
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-              <DiffusionCoefficient>NaN</DiffusionCoefficient>
-              <DynamicProperties />
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-            <Compound>
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-              <ComponentName>Water</ComponentName>
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-          <Name>Liquid2</Name>
-          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
-            <gibbs_free_energy>0</gibbs_free_energy>
-            <helmholtz_energy>0</helmholtz_energy>
-            <internal_energy>0</internal_energy>
-            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>0</molar_helmholtz_energy>
-            <molar_internal_energy>0</molar_internal_energy>
-          </Properties>
-        </Phase>
-        <Phase>
-          <ID>5</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Oxygen</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
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-              <Molarity>0</Molarity>
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-              <FugacityCoeff>0</FugacityCoeff>
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-              <lnKvalue>0</lnKvalue>
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-              <Name>Oxygen</Name>
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-              <PartialVolume>0</PartialVolume>
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-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Acetic acid</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
-              <MoleFraction>0</MoleFraction>
-              <Molarity>0</Molarity>
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-              <FugacityCoeff>0</FugacityCoeff>
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-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>Acetic acid</Name>
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-              <PartialVolume>0</PartialVolume>
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-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>P-xylene</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
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-              <Name>P-xylene</Name>
-              <PartialPressure>0</PartialPressure>
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-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Terephthalic acid</ComponentName>
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-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
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-              <Name>Terephthalic acid</Name>
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-              <PartialVolume>0</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Water</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
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-              <Name>Water</Name>
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-              <PartialVolume>0</PartialVolume>
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-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-          </Compounds>
-          <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
-          <ComponentDescription></ComponentDescription>
-          <ComponentName>Liquid3</ComponentName>
-          <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
-          <Name>Liquid3</Name>
-          <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
-          <Properties>
-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
-            <gibbs_free_energy>0</gibbs_free_energy>
-            <helmholtz_energy>0</helmholtz_energy>
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-            <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
-            <molar_helmholtz_energy>0</molar_helmholtz_energy>
-            <molar_internal_energy>0</molar_internal_energy>
-          </Properties>
-        </Phase>
-        <Phase>
-          <ID>6</ID>
-          <Compounds>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Oxygen</ComponentName>
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-              <Name>Oxygen</Name>
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-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Acetic acid</ComponentName>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
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-              <MassFlow>0</MassFlow>
-              <MolarFlow>0</MolarFlow>
-              <Name>P-xylene</Name>
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-              <PartialVolume>0</PartialVolume>
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-              <VolumetricFraction>0</VolumetricFraction>
-              <DiffusionCoefficient>0</DiffusionCoefficient>
-              <DynamicProperties />
-            </Compound>
-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Terephthalic acid</ComponentName>
-              <ActivityCoeff>0</ActivityCoeff>
-              <PetroleumFraction>false</PetroleumFraction>
-              <MassFraction>0</MassFraction>
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-              <Name>Terephthalic acid</Name>
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-              <DynamicProperties />
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-            <Compound>
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-              <ComponentName>Water</ComponentName>
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-              <Name>Water</Name>
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-          <ComponentName>Aqueous</ComponentName>
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-            <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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-            <molar_internal_energy>0</molar_internal_energy>
-          </Properties>
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-        <Phase>
-          <ID>7</ID>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
-              <ComponentDescription></ComponentDescription>
-              <ComponentName>Oxygen</ComponentName>
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-              <FugacityCoeff>NaN</FugacityCoeff>
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-              <Name>Oxygen</Name>
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-              <DynamicProperties />
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <ComponentName>Acetic acid</ComponentName>
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-              <FugacityCoeff>NaN</FugacityCoeff>
-              <Kvalue>0</Kvalue>
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-              <MassFlow>0</MassFlow>
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-            <Compound>
-              <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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-              <FugacityCoeff>NaN</FugacityCoeff>
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-              <Name>P-xylene</Name>
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-              <FugacityCoeff>NaN</FugacityCoeff>
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-          <PropertyType>System.String</PropertyType>
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-        <Property>
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-      <AttachedUtilities />
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-        <PropertyID Value="PROP_AC_2" />
-      </ObjectType>
-      <ObjectType Value="Adjust">
-        <PropertyID Value="MinVal" />
-        <PropertyID Value="MaxVal" />
-        <PropertyID Value="AdjustValue" />
-        <PropertyID Value="Tolerance" />
-        <PropertyID Value="StepSize" />
-        <PropertyID Value="MaximumIterations" />
-      </ObjectType>
-      <ObjectType Value="AnalogGauge" />
-      <ObjectType Value="CapeOpenUO" />
-      <ObjectType Value="ComponentSeparator">
-        <PropertyID Value="PROP_CP_0" />
-        <PropertyID Value="SpecifiedStreamIndex" />
-      </ObjectType>
-      <ObjectType Value="Compressor">
-        <PropertyID Value="PROP_CO_0" />
-        <PropertyID Value="PROP_CO_1" />
-        <PropertyID Value="PROP_CO_2" />
-        <PropertyID Value="PROP_CO_3" />
-        <PropertyID Value="PROP_CO_4" />
-        <PropertyID Value="PolytropicEfficiency" />
-        <PropertyID Value="AdiabaticCoefficient" />
-        <PropertyID Value="PolytropicCoefficient" />
-        <PropertyID Value="AdiabaticHead" />
-        <PropertyID Value="PolytropicHead" />
-        <PropertyID Value="RotationSpeed" />
-      </ObjectType>
-      <ObjectType Value="Cooler">
-        <PropertyID Value="Flow Conductance" />
-        <PropertyID Value="Volume" />
-        <PropertyID Value="Minimum Pressure" />
-        <PropertyID Value="Initialize using Inlet Stream" />
-        <PropertyID Value="Reset Content" />
-        <PropertyID Value="PROP_CL_0" />
-        <PropertyID Value="PROP_CL_1" />
-        <PropertyID Value="PROP_CL_2" />
-        <PropertyID Value="PROP_CL_3" />
-        <PropertyID Value="PROP_CL_4" />
-        <PropertyID Value="PROP_CL_5" />
-      </ObjectType>
-      <ObjectType Value="CustomUO" />
-      <ObjectType Value="DigitalGauge" />
-      <ObjectType Value="DistillationColumn">
-        <PropertyID Value="PROP_DC_0" />
-        <PropertyID Value="PROP_DC_1" />
-        <PropertyID Value="PROP_DC_2" />
-        <PropertyID Value="PROP_DC_3" />
-        <PropertyID Value="PROP_DC_4" />
-        <PropertyID Value="PROP_DC_5" />
-        <PropertyID Value="PROP_DC_6" />
-        <PropertyID Value="PROP_DC_7" />
-        <PropertyID Value="Condenser_Specification_Value" />
-        <PropertyID Value="Reboiler_Specification_Value" />
-        <PropertyID Value="Global_Stage_Efficiency" />
-        <PropertyID Value="Condenser_Calculated_Value" />
-        <PropertyID Value="Reboiler_Calculated_Value" />
-      </ObjectType>
-      <ObjectType Value="EnergyRecycle">
-        <PropertyID Value="PROP_ER_0" />
-        <PropertyID Value="PROP_ER_1" />
-        <PropertyID Value="PROP_ER_2" />
-      </ObjectType>
-      <ObjectType Value="EnergyStream">
-        <PropertyID Value="PROP_ES_0" />
-      </ObjectType>
-      <ObjectType Value="ExcelUO">
-        <PropertyID Value="Calc_dQ" />
-      </ObjectType>
-      <ObjectType Value="Expander">
-        <PropertyID Value="PROP_TU_0" />
-        <PropertyID Value="PROP_TU_1" />
-        <PropertyID Value="PROP_TU_2" />
-        <PropertyID Value="PROP_TU_3" />
-        <PropertyID Value="PROP_TU_4" />
-        <PropertyID Value="PolytropicEfficiency" />
-        <PropertyID Value="AdiabaticCoefficient" />
-        <PropertyID Value="PolytropicCoefficient" />
-        <PropertyID Value="AdiabaticHead" />
-        <PropertyID Value="PolytropicHead" />
-        <PropertyID Value="RotationSpeed" />
-      </ObjectType>
-      <ObjectType Value="Filter">
-        <PropertyID Value="PROP_FT_0" />
-        <PropertyID Value="PROP_FT_1" />
-        <PropertyID Value="PROP_FT_2" />
-        <PropertyID Value="PROP_FT_3" />
-        <PropertyID Value="PROP_FT_4" />
-        <PropertyID Value="PROP_FT_5" />
-        <PropertyID Value="PROP_FT_6" />
-        <PropertyID Value="PROP_FT_7" />
-      </ObjectType>
-      <ObjectType Value="Flowsheet" />
-      <ObjectType Value="Heater">
-        <PropertyID Value="Flow Conductance" />
-        <PropertyID Value="Volume" />
-        <PropertyID Value="Minimum Pressure" />
-        <PropertyID Value="Initialize using Inlet Stream" />
-        <PropertyID Value="Reset Content" />
-        <PropertyID Value="PROP_HT_0" />
-        <PropertyID Value="PROP_HT_1" />
-        <PropertyID Value="PROP_HT_2" />
-        <PropertyID Value="PROP_HT_3" />
-        <PropertyID Value="PROP_HT_4" />
-        <PropertyID Value="PROP_HT_5" />
-      </ObjectType>
-      <ObjectType Value="HeatExchanger">
-        <PropertyID Value="PROP_HX_0" />
-        <PropertyID Value="PROP_HX_1" />
-        <PropertyID Value="PROP_HX_2" />
-        <PropertyID Value="PROP_HX_3" />
-        <PropertyID Value="PROP_HX_4" />
-        <PropertyID Value="PROP_HX_25" />
-        <PropertyID Value="PROP_HX_26" />
-        <PropertyID Value="PROP_HX_27" />
-        <PropertyID Value="PROP_HX_28" />
-      </ObjectType>
-      <ObjectType Value="Input" />
-      <ObjectType Value="LevelGauge" />
-      <ObjectType Value="MaterialStream">
-        <PropertyID Value="PROP_MS_0" />
-        <PropertyID Value="PROP_MS_1" />
-        <PropertyID Value="PROP_MS_2" />
-        <PropertyID Value="PROP_MS_3" />
-        <PropertyID Value="PROP_MS_4" />
-        <PropertyID Value="PROP_MS_9" />
-        <PropertyID Value="PROP_MS_10" />
-        <PropertyID Value="PROP_MS_27" />
-        <PropertyID Value="PROP_MS_130" />
-        <PropertyID Value="PROP_MS_154" />
-      </ObjectType>
-      <ObjectType Value="Mixer" />
-      <ObjectType Value="OrificePlate">
-        <PropertyID Value="PROP_OP_0" />
-        <PropertyID Value="PROP_OP_1" />
-        <PropertyID Value="PROP_OP_2" />
-        <PropertyID Value="PROP_OP_3" />
-        <PropertyID Value="PROP_OP_4" />
-        <PropertyID Value="PROP_OP_5" />
-        <PropertyID Value="PROP_OP_6" />
-        <PropertyID Value="PROP_OP_7" />
-      </ObjectType>
-      <ObjectType Value="PIDController">
-        <PropertyID Value="Active" />
-        <PropertyID Value="ManualOverride" />
-        <PropertyID Value="LastError" />
-        <PropertyID Value="CurrentError" />
-        <PropertyID Value="CumulativeError" />
-        <PropertyID Value="SetPoint" />
-        <PropertyID Value="SetPointAbs" />
-        <PropertyID Value="Kp" />
-        <PropertyID Value="Ki" />
-        <PropertyID Value="Kd" />
-        <PropertyID Value="Output" />
-        <PropertyID Value="OutputMin" />
-        <PropertyID Value="OutputMax" />
-        <PropertyID Value="OutputAbs" />
-      </ObjectType>
-      <ObjectType Value="Pipe">
-        <PropertyID Value="PROP_PS_0" />
-        <PropertyID Value="PROP_PS_1" />
-        <PropertyID Value="PROP_PS_2" />
-        <PropertyID Value="PROP_PS_8" />
-        <PropertyID Value="PROP_PS_9" />
-      </ObjectType>
-      <ObjectType Value="Pump">
-        <PropertyID Value="PROP_PU_0" />
-        <PropertyID Value="PROP_PU_1" />
-        <PropertyID Value="PROP_PU_2" />
-        <PropertyID Value="PROP_PU_3" />
-        <PropertyID Value="PROP_PU_4" />
-        <PropertyID Value="PROP_PU_5" />
-      </ObjectType>
-      <ObjectType Value="Reactor_Conversion">
-        <PropertyID Value="PROP_CR_0" />
-        <PropertyID Value="Calculation Mode" />
-      </ObjectType>
-      <ObjectType Value="Reactor_CSTR">
-        <PropertyID Value="Operating Pressure" />
-        <PropertyID Value="Liquid Level" />
-        <PropertyID Value="Height" />
-        <PropertyID Value="Minimum Pressure" />
-        <PropertyID Value="Initialize using Inlet Stream" />
-        <PropertyID Value="Reset Contents" />
-        <PropertyID Value="PROP_CS_0" />
-        <PropertyID Value="PROP_CS_1" />
-        <PropertyID Value="PROP_CS_2" />
-        <PropertyID Value="PROP_CS_3" />
-        <PropertyID Value="PROP_CS_4" />
-        <PropertyID Value="PROP_CS_5" />
-        <PropertyID Value="Calculation Mode" />
-      </ObjectType>
-      <ObjectType Value="Reactor_Equilibrium">
-        <PropertyID Value="PROP_EQ_0" />
-        <PropertyID Value="Calculation Mode" />
-        <PropertyID Value="Initial Gibbs Energy" />
-        <PropertyID Value="Final Gibbs Energy" />
-      </ObjectType>
-      <ObjectType Value="Reactor_Gibbs">
-        <PropertyID Value="PROP_GR_0" />
-        <PropertyID Value="PROP_GR_1" />
-        <PropertyID Value="Calculation Mode" />
-        <PropertyID Value="Initial Gibbs Energy" />
-        <PropertyID Value="Final Gibbs Energy" />
-        <PropertyID Value="Element Balance Residue" />
-      </ObjectType>
-      <ObjectType Value="Reactor_PFR">
-        <PropertyID Value="Max Sections" />
-        <PropertyID Value="Reset Contents" />
-        <PropertyID Value="PROP_PF_0" />
-        <PropertyID Value="PROP_PF_1" />
-        <PropertyID Value="PROP_PF_2" />
-        <PropertyID Value="PROP_PF_3" />
-        <PropertyID Value="PROP_PF_4" />
-        <PropertyID Value="PROP_PF_5" />
-        <PropertyID Value="PROP_PF_6" />
-        <PropertyID Value="PROP_PF_7" />
-        <PropertyID Value="PROP_PF_8" />
-        <PropertyID Value="Calculation Mode" />
-      </ObjectType>
-      <ObjectType Value="ReboiledAbsorber">
-        <PropertyID Value="PROP_RA_0" />
-        <PropertyID Value="PROP_RA_1" />
-        <PropertyID Value="PROP_RA_2" />
-        <PropertyID Value="PROP_RA_3" />
-        <PropertyID Value="PROP_RA_4" />
-      </ObjectType>
-      <ObjectType Value="Recycle">
-        <PropertyID Value="PROP_RY_0" />
-        <PropertyID Value="PROP_RY_1" />
-        <PropertyID Value="PROP_RY_2" />
-        <PropertyID Value="PROP_RY_3" />
-        <PropertyID Value="PROP_RY_4" />
-        <PropertyID Value="PROP_RY_5" />
-        <PropertyID Value="PROP_RY_6" />
-      </ObjectType>
-      <ObjectType Value="RefluxedAbsorber">
-        <PropertyID Value="PROP_RF_0" />
-        <PropertyID Value="PROP_RF_1" />
-        <PropertyID Value="PROP_RF_2" />
-        <PropertyID Value="PROP_RF_3" />
-        <PropertyID Value="PROP_RF_4" />
-        <PropertyID Value="PROP_RF_5" />
-        <PropertyID Value="PROP_RF_6" />
-      </ObjectType>
-      <ObjectType Value="ShortcutColumn">
-        <PropertyID Value="PROP_SC_0" />
-        <PropertyID Value="PROP_SC_1" />
-        <PropertyID Value="PROP_SC_2" />
-        <PropertyID Value="PROP_SC_3" />
-        <PropertyID Value="PROP_SC_4" />
-        <PropertyID Value="PROP_SC_5" />
-        <PropertyID Value="PROP_SC_6" />
-        <PropertyID Value="PROP_SC_7" />
-        <PropertyID Value="PROP_SC_8" />
-        <PropertyID Value="PROP_SC_9" />
-        <PropertyID Value="PROP_SC_10" />
-        <PropertyID Value="PROP_SC_11" />
-        <PropertyID Value="PROP_SC_12" />
-        <PropertyID Value="PROP_SC_13" />
-        <PropertyID Value="PROP_SC_14" />
-      </ObjectType>
-      <ObjectType Value="SolidsSeparator">
-        <PropertyID Value="PROP_SS_1" />
-        <PropertyID Value="PROP_SS_2" />
-      </ObjectType>
-      <ObjectType Value="Spec">
-        <PropertyID Value="SpecMin" />
-        <PropertyID Value="SpecMax" />
-        <PropertyID Value="Expression" />
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-      <ObjectType Value="Splitter">
-        <PropertyID Value="PROP_SP_1" />
-        <PropertyID Value="PROP_SP_2" />
-      </ObjectType>
-      <ObjectType Value="Switch" />
-      <ObjectType Value="Tank">
-        <PropertyID Value="Liquid Level" />
-        <PropertyID Value="Height" />
-        <PropertyID Value="Initialize using Inlet Stream" />
-        <PropertyID Value="Reset Content" />
-        <PropertyID Value="PROP_TK_0" />
-        <PropertyID Value="PROP_TK_1" />
-        <PropertyID Value="PROP_TK_2" />
-      </ObjectType>
-      <ObjectType Value="Valve">
-        <PropertyID Value="PROP_VA_0" />
-        <PropertyID Value="PROP_VA_1" />
-        <PropertyID Value="PROP_VA_2" />
-        <PropertyID Value="PROP_VA_3" />
-        <PropertyID Value="PROP_VA_4" />
-        <PropertyID Value="PROP_VA_5" />
-      </ObjectType>
-      <ObjectType Value="Vessel">
-        <PropertyID Value="Vessel Orientation" />
-        <PropertyID Value="Operating Pressure" />
-        <PropertyID Value="Liquid Level" />
-        <PropertyID Value="Volume" />
-        <PropertyID Value="Height" />
-        <PropertyID Value="Minimum Pressure" />
-        <PropertyID Value="Initialize using Inlet Stream" />
-        <PropertyID Value="Reset Content" />
-        <PropertyID Value="PROP_SV_0" />
-        <PropertyID Value="PROP_SV_1" />
-      </ObjectType>
-    </VisibleProperties>
-    <FlashAlgorithms>
-      <FlashAlgorithm>
-        <ID>Nested Loops (VLE)</ID>
-        <Type>DWSIM.Thermodynamics.PropertyPackages.Auxiliary.FlashAlgorithms.NestedLoops</Type>
-        <LimitVaporFraction>true</LimitVaporFraction>
-        <AlgoType>Nested_Loops_VLE</AlgoType>
-        <Description>Flash Algorithm for Vapor-Liquid Equilibria based on the Rachford-Rice VLE equations.</Description>
-        <Name>Nested Loops (VLE)</Name>
-        <MobileCompatible>true</MobileCompatible>
-        <Order>1</Order>
-        <StabSearchSeverity>0</StabSearchSeverity>
-        <InternalUseOnly>false</InternalUseOnly>
-        <Tag>Nested Loops (VLE)</Tag>
-        <FlashSettings>
-          <Setting Name="Replace_PTFlash" Value="False" />
-          <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" />
-          <Setting Name="PVFlash_MaximumTemperatureChange" Value="10" />
-          <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" />
-        </FlashSettings>
-      </FlashAlgorithm>
-      <FlashAlgorithm>
-        <ID>Nested Loops (SVLE - Eutectic) (2)</ID>
-        <Type>DWSIM.Thermodynamics.PropertyPackages.Auxiliary.FlashAlgorithms.NestedLoopsSLE</Type>
-        <SolidSolution>false</SolidSolution>
-        <AlgoType>Nested_Loops_SLE_Eutectic</AlgoType>
-        <Description>Flash Algorithm for Vapor-Solid-Liquid (VSLE) systems</Description>
-        <Name>Nested Loops (SVLE - Eutectic)</Name>
-        <MobileCompatible>false</MobileCompatible>
-        <Order>3</Order>
-        <StabSearchSeverity>0</StabSearchSeverity>
-        <InternalUseOnly>false</InternalUseOnly>
-        <Tag>Nested Loops (SVLE - Eutectic) (2)</Tag>
-        <FlashSettings>
-          <Setting Name="Replace_PTFlash" Value="False" />
-          <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" />
-          <Setting Name="PVFlash_MaximumTemperatureChange" Value="10" />
-          <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" />
-        </FlashSettings>
-      </FlashAlgorithm>
-    </FlashAlgorithms>
-  </Settings>
-  <DynamicProperties />
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-      <GradientMode>true</GradientMode>
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-      <Calculated>true</Calculated>
-      <Active>true</Active>
-      <Description>Material Stream</Description>
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-      <ObjectType>MaterialStream</ObjectType>
-      <Shape>0</Shape>
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-      <Status>Calculated</Status>
-      <AutoSize>false</AutoSize>
-      <Height>20</Height>
-      <IsConnector>false</IsConnector>
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-      <InputConnectors>
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-      <Calculated>true</Calculated>
-      <Active>true</Active>
-      <Description>Material Stream</Description>
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-      <Status>Calculated</Status>
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-      <IsConnector>false</IsConnector>
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-      <Y>265</Y>
-      <Selected>false</Selected>
-      <Rotation>0</Rotation>
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-      </EnergyConnector>
-      <SpecialConnectors />
-    </GraphicObject>
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-      <GradientMode>true</GradientMode>
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-      <Active>true</Active>
-      <Description>Material Stream</Description>
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-      <FlippedV>false</FlippedV>
-      <IsEnergyStream>false</IsEnergyStream>
-      <ObjectType>MaterialStream</ObjectType>
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-      <Status>Calculated</Status>
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-      <Name>MAT-f761e466-025d-4a4e-bd28-5c3e703eaa91</Name>
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-      <Y>317</Y>
-      <Selected>false</Selected>
-      <Rotation>0</Rotation>
-      <InputConnectors>
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-      <SpecialConnectors />
-    </GraphicObject>
-    <GraphicObject>
-      <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.HeaterGraphic</Type>
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-      <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
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-      <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
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-      <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
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-      <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
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-    &lt;DockWindow ID="2" DockState="DockRight" ZOrderIndex="4"&gt;
-      &lt;NestedPanes Count="0" /&gt;
-    &lt;/DockWindow&gt;
-    &lt;DockWindow ID="3" DockState="DockTop" ZOrderIndex="5"&gt;
-      &lt;NestedPanes Count="0" /&gt;
-    &lt;/DockWindow&gt;
-    &lt;DockWindow ID="4" DockState="DockBottom" ZOrderIndex="2"&gt;
-      &lt;NestedPanes Count="2"&gt;
-        &lt;Pane ID="0" RefID="2" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
-        &lt;Pane ID="1" RefID="1" PrevPane="2" Alignment="Left" Proportion="0.738161559888579" /&gt;
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-    &lt;/DockWindow&gt;
-  &lt;/DockWindows&gt;
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-    &lt;/FloatWindow&gt;
-  &lt;/FloatWindows&gt;
-&lt;/DockPanel&gt;</PanelLayout>
-</DWSIM_Simulation_Data>
-\ No newline at end of file
diff --git a/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Abstarct_Flowsheet_submission.pdf b/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Abstarct_Flowsheet_submission.pdf
new file mode 100644
index 0000000..3750bdd
--- /dev/null
+++ b/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Abstarct_Flowsheet_submission.pdf
diff --git a/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Propane_Propylene_MVR.dwxmz b/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Propane_Propylene_MVR.dwxmz
new file mode 100644
index 0000000..2babe5b
--- /dev/null
+++ b/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/Propane_Propylene_MVR.dwxmz
diff --git a/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/README.txt b/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/README.txt
new file mode 100644
index 0000000..0bf88f2
--- /dev/null
+++ b/Propylene-Propane_Separation_Using_Mechanical_Vapor_Recompression_By_Mr_Mehulkumar_Sutariya/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Propylene-Propane Separation using Mechanical Vapor Recompression
+Proposar Name: Mr Mehulkumar Sutariya
+University: Sardar Vallabhbhai National Institute of Technology, Surat
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionabstractconverted.pdf b/Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionabstractconverted.pdf
deleted file mode 100644
index 4502af8..0000000
--- a/Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionabstractconverted.pdf
+++ /dev/null
diff --git a/Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionprocessfortherecoveryoffreshwater.dwxmz b/Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionprocessfortherecoveryoffreshwater.dwxmz
deleted file mode 100644
index 773912c..0000000
--- a/Purification_Of_Saline_Water_By_Mr_B_Dai_Mukesh_Reddy/Vaporrecompressionprocessfortherecoveryoffreshwater.dwxmz
+++ /dev/null
diff --git a/Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Group_9_Simulation_Description.pdf b/Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Group_9_Simulation_Description.pdf
deleted file mode 100644
index 9dca031..0000000
--- a/Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Group_9_Simulation_Description.pdf
+++ /dev/null
diff --git a/Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Sulfuric_acid_process_GroupAtul.dwxmz b/Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Sulfuric_acid_process_GroupAtul.dwxmz
deleted file mode 100644
index 0425806..0000000
--- a/Sulphuric_Acid_Process_Flowsheet_By_Ms_Swarali_Ghodkhande/Sulfuric_acid_process_GroupAtul.dwxmz
+++ /dev/null
diff --git a/Synthesis_Of_Ammonia_In_Cryogenic_Process_By_Mr_Yash_Shankar_Chikorde/README.txt b/Synthesis_Of_Ammonia_In_Cryogenic_Process_By_Mr_Yash_Shankar_Chikorde/README.txt
new file mode 100644
index 0000000..b902d3b
--- /dev/null
+++ b/Synthesis_Of_Ammonia_In_Cryogenic_Process_By_Mr_Yash_Shankar_Chikorde/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Synthesis of Ammonia in Cryogenic Process
+Proposar Name: Mr Yash Shankar Chikorde
+University:  KLE Dr. M. S. Sheshgiri College of Engineering and Technology, Belagavi
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Abstract_Ethanol.pdf b/Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Abstract_Ethanol.pdf
deleted file mode 100644
index 2845f5d..0000000
--- a/Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Abstract_Ethanol.pdf
+++ /dev/null
diff --git a/Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Ethanol_Flowsheet.dwxmz b/Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Ethanol_Flowsheet.dwxmz
deleted file mode 100644
index 07700ad..0000000
--- a/Synthesis_Of_Ethyl_Alcohol_From_Ethylene_By_Ms_Yukta_Bhange/Ethanol_Flowsheet.dwxmz
+++ /dev/null
diff --git a/Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.dwxmz b/Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.dwxmz
deleted file mode 100644
index c67504c..0000000
--- a/Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.dwxmz
+++ /dev/null
diff --git a/Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.pdf b/Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.pdf
deleted file mode 100644
index 542339e..0000000
--- a/Tame_Production_Using_Reactive_Distillation_And_Pressure_Swing_Column_By_Mr_Gaurav_Tiwari/TAME.pdf
+++ /dev/null
diff --git a/Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/Abstract_tcpsed.pdf b/Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/Abstract_tcpsed.pdf
deleted file mode 100644
index e799444..0000000
--- a/Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/Abstract_tcpsed.pdf
+++ /dev/null
diff --git a/Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/triple_column_pressureswing_with_extractive_distillation.dwxmz b/Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/triple_column_pressureswing_with_extractive_distillation.dwxmz
deleted file mode 100644
index 2674d28..0000000
--- a/Triple_Column_Pressure_Swing_With_Extractive_Distillation_For_Methyl_Acetate-Methanol-Water_Separation_Figure_6_By_Ms_Ankita_Karkera/triple_column_pressureswing_with_extractive_distillation.dwxmz
+++ /dev/null
author	Sashi20	2021-12-16 00:20:14 +0550
committer	Sashi20	2021-12-16 00:20:14 +0550
commit	09bbc1651ae4ec837399f820ead3ca445b0bd31e (patch)
tree	851610cec92a2eff5aa07388ff86fda72a0f4ce7
parent	02b340799399458167d550feee1286978aeda61b (diff)
download	DWSIM-Flowsheets-09bbc1651ae4ec837399f820ead3ca445b0bd31e.tar.gz DWSIM-Flowsheets-09bbc1651ae4ec837399f820ead3ca445b0bd31e.tar.bz2 DWSIM-Flowsheets-09bbc1651ae4ec837399f820ead3ca445b0bd31e.zip