From 2e7a5d27c66245d608729bf40fb8d867ed9293c5 Mon Sep 17 00:00:00 2001 From: Sashi20 Date: Fri, 22 Mar 2024 17:53:56 +0550 Subject: Added(A)/Deleted(D) following Flowsheet file M A_Simple_De-Humidification_System_By_Mr_Kaushik_Datta/Abstract_A_Simple_Dehumidification_System.pdf M A_Simple_De-Humidification_System_By_Mr_Kaushik_Datta/README.txt M A_Simple_De-Humidification_System_By_Mr_Kaushik_Datta/dehumidification.mo M Acetic_Acid_Esterification_By_Ethanol_By_Mr_Pravin_Dalve/Acetic_Acid_Esterification_by_Ethanol.mo M Acetic_Acid_Esterification_By_Ethanol_By_Mr_Pravin_Dalve/README.txt M Acetic_Acid_Esterification_By_Ethanol_By_Mr_Pravin_Dalve/Simulator.mo M Acetic_Acid_Esterification_By_Ethanol_By_Mr_Pravin_Dalve/esterification.pdf M Benzene_Toluene_Fractionation_Unit_By_Mr_Kedar_H_Joshi/Abstract_BenzeneTolueneDistillation.pdf M Benzene_Toluene_Fractionation_Unit_By_Mr_Kedar_H_Joshi/Flowsheet_BenzeneTolueneDistillation.mo M Benzene_Toluene_Fractionation_Unit_By_Mr_Kedar_H_Joshi/README.txt M Btx_Separation_Chain_And_Energy_Optimization_By_Mr_Mehulkumar_Sutariya/BTX.mo M Btx_Separation_Chain_And_Energy_Optimization_By_Mr_Mehulkumar_Sutariya/README.txt M Btx_Separation_Chain_And_Energy_Optimization_By_Mr_Mehulkumar_Sutariya/report.pdf M Camere_Process_By_Mr_Mehulkumar_Sutariya/CAMERE.mo M Camere_Process_By_Mr_Mehulkumar_Sutariya/Camere_Process.pdf M Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/IsobutaneNew.mo M Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/README.txt M Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/EthanolDehydrationNew.mo M Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/README.txt M 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Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/README.txt M Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/flowsheet3.mo M Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/Abstract.pdf M Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/README.txt M Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/thermodynamic.mo A Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Abstract_EthanolExtractiveDistillation_Using_Mixed_Glycols.pdf A Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Flowsheet_EthanolExtractiveDistillation_Using_Mixed_Glycols.mo M Ethylene_Glycol_Production_By_Mr_Rahul_A_S/Ethylene_Glycol_Production.pdf M Ethylene_Glycol_Production_By_Mr_Rahul_A_S/Flowsheet_Final.mo M Ethylene_Glycol_Production_By_Mr_Rahul_A_S/README.txt D Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/ExtrDist.mo D Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/extrDist.pdf A Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Extractive_Distillation_of_EthylAcetate_and_Cyclohexane_Mixture.pdf A Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Flow.mo A Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/README.txt M Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/Abstract_ExtractiveDistillationofTHFandEthanol.pdf M Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/Flowsheet_extractive_distillation_of_ethylene_glycol.mo M Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/README.txt A Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Abstract_Synthesis_of_Isobutane_form_butane.pdf A Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Isomerisation.mo M Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Abstract.pdf M Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Methanol_Water_Sep.mo M Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/README.txt M Methanol_Water_Distillation_By_Mr_Rahul_A_S/Methanol_Water.pdf M Methanol_Water_Distillation_By_Mr_Rahul_A_S/Methanol_Water_Distillation.mo M Methanol_Water_Distillation_By_Mr_Rahul_A_S/README.txt M Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/MethanolWaterDistillatioWithPreheating.pdf M Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/MethanolWaterDistillationWithPreheating.mo M Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/README.txt M Methyl_Acetate_Process_Using_Carbonylation_Of_Dimethyl_Ether_Produced_From_Methanol_By_Ms_Trisha_Dutta/Abstract_Carbonylation_of_DME.pdf M Methyl_Acetate_Process_Using_Carbonylation_Of_Dimethyl_Ether_Produced_From_Methanol_By_Ms_Trisha_Dutta/Carbonylation_of_DME.mo M Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/Nitrogen_Liquefaction.mo M Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/Nitrogen_Liquefaction_Linde_Cycle.pdf M Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/README.txt M Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/Abstract.pdf M Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/README.txt M Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/openloopturbine.mo A Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Abstract_Separation_of_methanol_and_diethylamine.pdf A Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Separation_of_Diethylamine_and_Methanol.mo M Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/PSD.mo M Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/README.txt M Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Abstract_PSDMeth.pdf M Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Flowsheet_PSDMeth.mo M Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/README.txt M "Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/Abstract.pdf" M "Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/PSD_EA_EO.mo" M "Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/README.txt" A Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Abstract_Separation_Of_Ethyl_Acetate_And_Cyclohexane_using_PSD.pdf A Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Flowsheet_PSD.mo A Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/README.txt M Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/Abstract.pdf M Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/Flowsheet_PSDMethanol.mo M Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/README.txt M Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/PSDwithRecycle.mo M Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/README.txt M Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Abstract.pdf M Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Flowsheet_PSDWater.mo M Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/README.txt M Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/Flowsheet_PSDEthyl.mo M Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/README.txt M Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/abstract.pdf M Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Abstract.pdf M Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Flowsheet_PSDIsobutanol.mo M Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/README.txt M Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/Abstract_PSD_Toluene_Ethanol.pdf M Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/PSD.mo M Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/README.txt M Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/PSD_Abstract.pdf M Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/PresSwingDist.mo M Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/README.txt M Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/Abstract_PSD.pdf M Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/Flowsheet_PSD.mo M Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/README.txt M Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/OpenModelica_Flowsheeting_Project_Abstract_v01_31Oct2019.pdf M Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/Process_Development_for_the_Production_of_Propylene_Oxide.mo M Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/README.txt A Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Abstract.pdf A Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Ethylbenzene.mo A Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/README.txt M Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/AceticAcidAbstract.pdf M Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/README.txt M Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/aceticacid.mo M Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid.mo M Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid_Abstract.pdf M Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/README.txt M Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/Ammonia.mo M Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/AmmoniaAbs.pdf M Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/README.txt M Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/README.txt M Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/ammonia.pdf M Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/ammonia_by_haber_new.mo A Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/Abstract_ButanalProduction.pdf A Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/butanal.mo A Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Chlorobenzene.mo A Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Production_of_Chlorobenzene.pdf A Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/README.txt M Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/Cumenewithrecycle.mo M Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/README.txt A Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheet.mo A Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheetAbstract.pdf A Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/README.txt M Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/Diethyl.mo M Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/README.txt M Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/abstract_diethylether.pdf M Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/Dimethylether_Production_Abstract.pdf M Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/Dimethylether_Production_Flowsheet.mo M Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/README.txt M Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/README.txt M Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/abstract.pdf M Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/ethylchloride.mo M Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/Abstract.pdf M Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/README.txt M Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/ethyleneOxide.mo A Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/Production_of_Hydrogen_using_WGRS.pdf A Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/README.txt A Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/wgrs.mo M Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/Methanation_System.pdf M Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/Methanation_system.mo M Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/README.txt M Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/README.txt M Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/methanolNew.mo A Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.mo A Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.pdf M Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/Flowsheet_ProductionOfParaxylene.mo M Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/README.txt M Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/abstract.pdf A Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Production_Of_Toluene_By_Dehydration_of_Normal_Heptane.pdf A Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/README.txt A Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Toluene.mo M Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/README.txt M Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/VinylChloride_Production_Abstract.pdf M Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/VinylChloride_Production_Flowsheet.mo M Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/Abstract.pdf M Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/MethanolTolueneExtractiveNew.mo M Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/README.txt A Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/Abstract.pdf A Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/flowsheet.mo M Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/Iso1.mo M Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/README.txt M Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/Tanay_Removal_of_Isopentane.pdf M Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/Abstract_OM.pdf M Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/Air_benzene_separation.mo M Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/README.txt A Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/Abstract_Separation_of_Pyridine_and_Water_using_PSD.pdf A Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/PSD.mo A Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/README.txt M Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/PSD1.mo M Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/PSD_abstract.pdf M 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Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Flowsheet_PSDMeth.mo mode change 100755 => 100644 Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/README.txt mode change 100755 => 100644 "Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/Abstract.pdf" mode change 100755 => 100644 "Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/PSD_EA_EO.mo" mode change 100755 => 100644 "Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/README.txt" create mode 100644 Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Abstract_Separation_Of_Ethyl_Acetate_And_Cyclohexane_using_PSD.pdf create mode 100644 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Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/README.txt mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Abstract.pdf mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Flowsheet_PSDWater.mo mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/README.txt mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/Flowsheet_PSDEthyl.mo mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/README.txt mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/abstract.pdf mode change 100755 => 100644 Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Abstract.pdf mode change 100755 => 100644 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Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Abstract.pdf create mode 100644 Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Ethylbenzene.mo create mode 100644 Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/README.txt mode change 100755 => 100644 Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/AceticAcidAbstract.pdf mode change 100755 => 100644 Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/README.txt mode change 100755 => 100644 Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/aceticacid.mo mode change 100755 => 100644 Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid.mo mode change 100755 => 100644 Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid_Abstract.pdf mode change 100755 => 100644 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a/Camere_Process_By_Mr_Mehulkumar_Sutariya/Camere_Process.pdf b/Camere_Process_By_Mr_Mehulkumar_Sutariya/Camere_Process.pdf old mode 100755 new mode 100644 diff --git a/Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/IsobutaneNew.mo b/Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/IsobutaneNew.mo old mode 100755 new mode 100644 diff --git a/Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/README.txt b/Conversion_Of_N-Butane_To_Isobutane_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/EthanolDehydrationNew.mo b/Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/EthanolDehydrationNew.mo old mode 100755 new mode 100644 diff --git a/Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/README.txt b/Dehydration_Of_Ethanol_Using_Glycerol_As_Entrainer_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Distillation_Of_Aqueous_Acetone_By_Mr_Kaushik_Datta/Abstract_Distillation_Of_Aqueous_Acetone.pdf b/Distillation_Of_Aqueous_Acetone_By_Mr_Kaushik_Datta/Abstract_Distillation_Of_Aqueous_Acetone.pdf old mode 100755 new mode 100644 diff --git a/Distillation_Of_Aqueous_Acetone_By_Mr_Kaushik_Datta/Aqueous_Acetone.mo b/Distillation_Of_Aqueous_Acetone_By_Mr_Kaushik_Datta/Aqueous_Acetone.mo old mode 100755 new mode 100644 diff --git a/Distillation_Of_Aqueous_Acetone_By_Mr_Kaushik_Datta/README.txt b/Distillation_Of_Aqueous_Acetone_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Abstract_DryMethaneReformingProcess.pdf b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Abstract_DryMethaneReformingProcess.pdf old mode 100755 new mode 100644 diff --git a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Flowsheet_DryMethaneReformingProcess.mo b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Flowsheet_DryMethaneReformingProcess.mo old mode 100755 new mode 100644 diff --git a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/README.txt b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/README.txt old mode 100755 new mode 100644 diff --git a/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Akshay_Kumar_Mehta/Abstract_EffectOfDistillationColumnSequenceOnSeparationOfCompounds.pdf b/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Akshay_Kumar_Mehta/Abstract_EffectOfDistillationColumnSequenceOnSeparationOfCompounds.pdf old mode 100755 new mode 100644 diff --git a/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Akshay_Kumar_Mehta/Flowsheet_EffectOfDistillationColumnSequenceOnSeparationOfCompounds.mo b/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Akshay_Kumar_Mehta/Flowsheet_EffectOfDistillationColumnSequenceOnSeparationOfCompounds.mo old mode 100755 new mode 100644 diff --git a/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Akshay_Kumar_Mehta/README.txt b/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Akshay_Kumar_Mehta/README.txt old mode 100755 new mode 100644 diff --git a/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/AbstractFlowsheet.pdf b/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/AbstractFlowsheet.pdf old mode 100755 new mode 100644 diff --git a/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/README.txt b/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/flowsheet3.mo b/Effect_Of_Column_Sequence_On_The_Separation_Of_Compounds_By_Mr_Malapati_Sree_Harsha/flowsheet3.mo old mode 100755 new mode 100644 diff --git a/Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/Abstract.pdf b/Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/README.txt b/Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/thermodynamic.mo b/Effect_Of_Thermodynamic_Models_On_Separation_Of_Aromatics_By_Mr_Malapati_Sree_Harsha/thermodynamic.mo old mode 100755 new mode 100644 diff --git a/Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Abstract_EthanolExtractiveDistillation_Using_Mixed_Glycols.pdf b/Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Abstract_EthanolExtractiveDistillation_Using_Mixed_Glycols.pdf new file mode 100644 index 0000000..e8bdb54 Binary files /dev/null and b/Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Abstract_EthanolExtractiveDistillation_Using_Mixed_Glycols.pdf differ diff --git a/Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Flowsheet_EthanolExtractiveDistillation_Using_Mixed_Glycols.mo b/Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Flowsheet_EthanolExtractiveDistillation_Using_Mixed_Glycols.mo new file mode 100644 index 0000000..3f5f60a --- /dev/null +++ b/Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Flowsheet_EthanolExtractiveDistillation_Using_Mixed_Glycols.mo @@ -0,0 +1,134 @@ +package Extraction + model flowsheet + // defination of the unit operations and streams used + import data = Simulator.Files.ChemsepDatabase; + parameter data.Ethanol Eth; + parameter data.Glycerol Gly; + parameter data.Ethyleneglycol Egly; + parameter data.Water h2o; + parameter Integer Nc = 4; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {Eth, h2o, Gly, Egly}; + Extraction.matstream Entrainer(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-174, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream Makeup(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-174, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer1(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-136, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream mixfeed(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-104, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream feed(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-174, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.Discolumn dist1(C = C, InT_s = {4, 12}, Nc = Nc, Ni = 2, Nt = 20) annotation( + Placement(visible = true, transformation(origin = {-40, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream D1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {10, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream B1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {8, -32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.Discolumn dist2(C = C, InT_s = {4}, Nc = Nc, Ni = 1, Nt = 8) annotation( + Placement(visible = true, transformation(origin = {76, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream D2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {134, 30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream B2(C = C, Nc = Nc, T(start = 486)) annotation( + Placement(visible = true, transformation(origin = {134, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {162, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve valve1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {240, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream recyclestream(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {278, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Extraction.matstream out(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {198, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation +//Feed stream + feed.P = 100000; + feed.T = 298.15; + feed.F_p[1] = 27.7778; + feed.x_pc[1, :] = {0.88, 0.12, 0, 0}; +//================================================================= +//recycle stream + Entrainer.P = 100000; + Entrainer.T = 333.15; + Entrainer.F_p[1] = 22.194; + Entrainer.x_pc[1, :] = {0.001, 0, 0.399, 0.6}; +//makeup + Makeup.P = 100000; + Makeup.T = 333.15; + Makeup.F_p[1] = 0.0278; + Makeup.x_pc[1, :] = {0, 0, 0, 1}; +//================================================================= +//distillation column + dist1.condenser.P = 100000; + dist1.reboiler.P = 100000; + dist1.RR = 0.5; + B1.x_pc[1, 4] = 0.515; +//D1.x_pc[1, 1] = 0.998; +//B1.F_p[1] = 25.7167; +// + dist2.condenser.P = 19998; + dist2.reboiler.P = 19998; + dist2.RR = 0.92; +// D2.x_pc[1, 2] = 0.9; + B2.x_pc[1, 4] = 0.6; +//================================================================= + valve1.Pout = 100000; + cooler1.Tout = 333.15; +//================================================================= + connect(Entrainer.Out, mixer1.In[1]) annotation( + Line(points = {{-164, 32}, {-164, 18}, {-146, 18}}, color = {0, 70, 70})); + connect(Makeup.Out, mixer1.In[2]) annotation( + Line(points = {{-164, 2}, {-146, 2}, {-146, 18}}, color = {0, 70, 70})); + connect(mixer1.Out, mixfeed.In) annotation( + Line(points = {{-126, 18}, {-114, 18}}, color = {0, 70, 70})); + connect(mixfeed.Out, dist1.In_s[1]) annotation( + Line(points = {{-94, 18}, {-82, 18}, {-82, -2}, {-65, -2}}, color = {0, 70, 70})); + connect(feed.Out, dist1.In_s[2]) annotation( + Line(points = {{-164, -38}, {-86, -38}, {-86, -2}, {-65, -2}}, color = {0, 70, 70})); + connect(dist1.Dist, D1.In) annotation( + Line(points = {{-15, 28}, {0, 28}}, color = {0, 70, 70})); + connect(dist1.Bot, B1.In) annotation( + Line(points = {{-15, -32}, {-2, -32}}, color = {0, 70, 70})); + connect(B1.Out, dist2.In_s[1]) annotation( + Line(points = {{18, -32}, {18, -14}, {32, -14}, {32, 0}, {51, 0}}, color = {0, 70, 70})); + connect(dist2.Dist, D2.In) annotation( + Line(points = {{101, 30}, {124, 30}}, color = {0, 70, 70})); + connect(dist2.Bot, B2.In) annotation( + Line(points = {{101, -30}, {124, -30}}, color = {0, 70, 70})); + connect(B2.Out, cooler1.In) annotation( + Line(points = {{144, -30}, {152, -30}}, color = {0, 70, 70})); + connect(valve1.Out, recyclestream.In) annotation( + Line(points = {{250, -30}, {268, -30}}, color = {0, 70, 70})); + connect(cooler1.Out, out.In) annotation( + Line(points = {{172, -30}, {190, -30}, {190, -30}, {188, -30}, {188, -30}}, color = {0, 70, 70})); + connect(out.Out, valve1.In) annotation( + Line(points = {{208, -30}, {230, -30}}, color = {0, 70, 70})); + annotation( + Diagram(coordinateSystem(extent = {{-200, -100}, {300, 100}})), + Icon(coordinateSystem(extent = {{-200, -100}, {300, 100}})));end flowsheet; + + model matstream + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end matstream; + + model Condensor + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Condensor; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Reboiler; + + model Discolumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end Discolumn; +end Extraction; diff --git a/Ethylene_Glycol_Production_By_Mr_Rahul_A_S/Ethylene_Glycol_Production.pdf b/Ethylene_Glycol_Production_By_Mr_Rahul_A_S/Ethylene_Glycol_Production.pdf old mode 100755 new mode 100644 diff --git a/Ethylene_Glycol_Production_By_Mr_Rahul_A_S/Flowsheet_Final.mo b/Ethylene_Glycol_Production_By_Mr_Rahul_A_S/Flowsheet_Final.mo old mode 100755 new mode 100644 diff --git a/Ethylene_Glycol_Production_By_Mr_Rahul_A_S/README.txt b/Ethylene_Glycol_Production_By_Mr_Rahul_A_S/README.txt old mode 100755 new mode 100644 diff --git a/Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/ExtrDist.mo b/Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/ExtrDist.mo deleted file mode 100644 index d0fc9cd..0000000 --- a/Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/ExtrDist.mo +++ /dev/null @@ -1,154 +0,0 @@ -package ExtrDist - model ms - extends Simulator.Streams.MaterialStream; - extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; - end ms; - - -model Flowsheet - extends Modelica.Icons.Example; - import data = Simulator.Files.ChemsepDatabase; - parameter Integer Nc = 3; - parameter data.Monochlorobenzene mcb; - parameter data.Acetone ace; - parameter data.Water wat; - parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {mcb, ace, wat}; - ExtrDist.ms S01(Nc = Nc, C = C) annotation( - Placement(visible = true, transformation(origin = {-150, 80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.ms S02(Nc = Nc, C = C) annotation( - Placement(visible = true, transformation(origin = {-210, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.DistColumn dist1(Nc = Nc, Ctype = "Total", C = C, Nt = 5, Ni = 2, InT_s = {2, 3}) annotation( - Placement(visible = true, transformation(origin = {-90, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.ms d1(Nc = Nc, C = C) annotation( - Placement(visible = true, transformation(origin = {-30, 56}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.ms b1(Nc = Nc, C = C) annotation( - Placement(visible = true, transformation(origin = {-28, -4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.DistColumn dist2(Nc = Nc, Ctype = "Total", C = C, Nt = 5, Ni = 1, InT_s = {2}) annotation( - Placement(visible = true, transformation(origin = {26, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.ms d2(Nc = Nc, C = C) annotation( - Placement(visible = true, transformation(origin = {88, 48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - ExtrDist.ms b2(Nc = Nc, C = C) annotation( - Placement(visible = true, transformation(origin = {88, -12}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - -equation - connect(S02.Out, dist1.In_s[1]) annotation( - Line(points = {{-200, 0}, {-118, 0}, {-118, 12}, {-120, 12}, {-120, 22}, {-114, 22}, {-114, 22}}, color = {0, 70, 70})); - connect(dist2.Bot, b2.In) annotation( - Line(points = {{52, -12}, {78, -12}, {78, -12}, {78, -12}}, color = {0, 70, 70})); - connect(dist2.Dist, d2.In) annotation( - Line(points = {{52, 48}, {78, 48}, {78, 48}, {78, 48}}, color = {0, 70, 70})); - connect(d1.Out, dist2.In_s[1]) annotation( - Line(points = {{-20, 56}, {-12, 56}, {-12, 18}, {0, 18}, {0, 18}, {2, 18}}, color = {0, 70, 70})); - connect(dist1.Dist, d1.In) annotation( - Line(points = {{-65, 52}, {-53.5, 52}, {-53.5, 56}, {-40, 56}}, color = {0, 70, 70})); - connect(S01.Out, dist1.In_s[2]) annotation( - Line(points = {{-140, 80}, {-120, 80}, {-120, 22}, {-115, 22}}, color = {0, 70, 70})); - connect(dist1.Bot, b1.In) annotation( - Line(points = {{-65, -8}, {-50.5, -8}, {-50.5, -4}, {-38, -4}}, color = {0, 70, 70})); - S01.x_pc[1, :] = {1, 0, 0}; - S01.T = 298.15; - S01.F_p[1] = 8.8844; - S01.P = 101325; - S02.x_pc[1, :] = {0.00000000086, 0.7067, 0.2933}; - S02.T = 306.832; - S02.F_p[1] = 27.5611; - S02.P = 101325; - dist1.condenser.P = 101325; - dist1.reboiler.P = 101325; - d1.x_pc[1, 2] = 0.8476; - b1.x_pc[1, 2] = 0.40; - dist2.condenser.P = 101325; - dist2.reboiler.P = 101325; - dist2.RR = 0.99; - b2.x_pc[1, 2] = 0.73112; - end Flowsheet; - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - - model Tray - extends Simulator.UnitOperations.DistillationColumn.DistTray; - extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; - end Tray; - - - model Reboiler - extends Simulator.UnitOperations.DistillationColumn.Reb; - extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; - end Reboiler; - - - model DistColumn - extends Simulator.UnitOperations.DistillationColumn.DistCol; - Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); - Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); - Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); - end DistColumn; - - model Condensor - extends Simulator.UnitOperations.DistillationColumn.Cond; - extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; - end Condensor; - - - - - - - -end ExtrDist; diff --git a/Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/extrDist.pdf b/Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/extrDist.pdf deleted file mode 100644 index c1dac7b..0000000 Binary files a/Extraction_Of_Acetone_From_An_Aqueous_Solution_Using_Monochlorobenzene_As_Solvent_By_Mr_Sandeep_Kumar_Samanta/extrDist.pdf and /dev/null differ diff --git a/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Extractive_Distillation_of_EthylAcetate_and_Cyclohexane_Mixture.pdf b/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Extractive_Distillation_of_EthylAcetate_and_Cyclohexane_Mixture.pdf new file mode 100644 index 0000000..e89fd64 Binary files /dev/null and b/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Extractive_Distillation_of_EthylAcetate_and_Cyclohexane_Mixture.pdf differ diff --git a/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Flow.mo b/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Flow.mo new file mode 100644 index 0000000..2f016fe --- /dev/null +++ b/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/Flow.mo @@ -0,0 +1,129 @@ +package Flow + model flowsheet + + import data = Simulator.Files.ChemsepDatabase; + + parameter data.Ethylacetate eth; + parameter data.Cyclohexane ch; + parameter data.Dimethylsulfoxide dms; + + parameter Integer Nc = 3; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {eth,ch,dms}; + Flow.matstream Entrainer(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-174, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream Makeup(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-174, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer1(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-136, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream mixfeed(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-104, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream feed(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-174, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.Discolumn dist1(C = C, InT_s = {8,10}, Nc = Nc, Ni = 2, Nt = 16) annotation( + Placement(visible = true, transformation(origin = {-40, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream D1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {10, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream B1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {8, -32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.Discolumn dist2(C = C, InT_s = {3}, Nc = Nc, Ni = 1, Nt = 6) annotation( + Placement(visible = true, transformation(origin = {76, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream D2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {134, 30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream B2(C = C, Nc = Nc,T(start=452)) annotation( + Placement(visible = true, transformation(origin = {134, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {168, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream Out(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {196, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve valve1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {234, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flow.matstream Recycle(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {272, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + + feed.P = 100000; + feed.T = 323.15; + feed.F_p[1] = 27.7778; + feed.x_pc[1, :] = {0.5,0.5,0}; + + Entrainer.P = 100000; + Entrainer.T = 323.15; + Entrainer.F_p[1] = 36.11; + Entrainer.x_pc[1, :] = {0.001,0,0.999}; + + Makeup.P = 100000; + Makeup.T = 323.15; + Makeup.F_p[1] = 0.02; + Makeup.x_pc[1, :] = {0,0,1}; + + dist1.condenser.P = 70000; + dist1.reboiler.P = 70000; + dist1.RR =1.5; + B1.x_pc[1, 2] = 0.0003; + + + dist2.condenser.P = 40000; + dist2.reboiler.P = 40000; + dist2.RR = 1; + B2.x_pc[1, 1] = 0.001; + + valve1.Pout = 100000; + cooler1.Tout = 323.15; + + connect(Entrainer.Out, mixer1.In[1]) annotation( + Line(points = {{-164, 32}, {-164, 18}, {-146, 18}}, color = {0, 70, 70})); + connect(Makeup.Out, mixer1.In[2]) annotation( + Line(points = {{-164, 2}, {-146, 2}, {-146, 18}}, color = {0, 70, 70})); + connect(mixer1.Out, mixfeed.In) annotation( + Line(points = {{-126, 18}, {-114, 18}}, color = {0, 70, 70})); + connect(mixfeed.Out, dist1.In_s[1]) annotation( + Line(points = {{-94, 18}, {-82, 18}, {-82, -2}, {-65, -2}}, color = {0, 70, 70})); + connect(feed.Out, dist1.In_s[2]) annotation( + Line(points = {{-164, -38}, {-86, -38}, {-86, -2}, {-65, -2}}, color = {0, 70, 70})); + connect(dist1.Dist, D1.In) annotation( + Line(points = {{-15, 28}, {0, 28}}, color = {0, 70, 70})); + connect(dist1.Bot, B1.In) annotation( + Line(points = {{-15, -32}, {-2, -32}}, color = {0, 70, 70})); + connect(B1.Out, dist2.In_s[1]) annotation( + Line(points = {{18, -32}, {18, -14}, {32, -14}, {32, 0}, {51, 0}}, color = {0, 70, 70})); + connect(dist2.Dist, D2.In) annotation( + Line(points = {{101, 30}, {124, 30}}, color = {0, 70, 70})); + connect(dist2.Bot, B2.In) annotation( + Line(points = {{101, -30}, {124, -30}}, color = {0, 70, 70})); + connect(B2.Out, cooler1.In) annotation( + Line(points = {{144, -30}, {158, -30}}, color = {0, 70, 70})); + connect(cooler1.Out, Out.In) annotation( + Line(points = {{178, -30}, {186, -30}, {186, -30}, {186, -30}}, color = {0, 70, 70})); + connect(Out.Out, valve1.In) annotation( + Line(points = {{206, -30}, {224, -30}}, color = {0, 70, 70})); + connect(valve1.Out,Recycle.In) annotation( + Line(points = {{244, -30}, {262, -30}}, color = {0, 70, 70})); + end flowsheet; + + model matstream + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end matstream; + + model Condensor + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Condensor; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Reboiler; + + model Discolumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end Discolumn; +end Flow; diff --git a/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/README.txt b/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/README.txt new file mode 100644 index 0000000..296e3f3 --- /dev/null +++ b/Extractive_Distillation_Of_Ethyl_Acetate_And_Cyclohexane_Mixture_By_Ms_Shanvi_Tiwari/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Extractive Distillation of ethyl acetate and cyclohexane mixture +Proposar Name: Ms Shanvi Tiwari +University: National Institute of Technology,Warangal + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/Abstract_ExtractiveDistillationofTHFandEthanol.pdf b/Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/Abstract_ExtractiveDistillationofTHFandEthanol.pdf old mode 100755 new mode 100644 diff --git a/Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/Flowsheet_extractive_distillation_of_ethylene_glycol.mo b/Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/Flowsheet_extractive_distillation_of_ethylene_glycol.mo old mode 100755 new mode 100644 diff --git a/Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/README.txt b/Extractive_Distillation_Of_Thf_And_Ethanol_Using_Ethylene_Glycol_By_Mr_Akshay_Kumar_Mehta/README.txt old mode 100755 new mode 100644 diff --git a/Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Abstract_Synthesis_of_Isobutane_form_butane.pdf b/Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Abstract_Synthesis_of_Isobutane_form_butane.pdf new file mode 100644 index 0000000..ec30ff4 Binary files /dev/null and b/Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Abstract_Synthesis_of_Isobutane_form_butane.pdf differ diff --git a/Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Isomerisation.mo b/Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Isomerisation.mo new file mode 100644 index 0000000..2a1c5c6 --- /dev/null +++ b/Isomerization_Of_N-Butane_To_Isobutane_And_Isopentane_By_Ms_Aayushi_Gupta/Isomerisation.mo @@ -0,0 +1,74 @@ +package Isomerisation + + model MS "Extending Material Stream with Raoult's Law" + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "
This is a non-executable model is created inside the package Mixer to extend the MaterialStream model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the MixerSimulation model to create the required number of instances of the material stream model.
")); + end MS; + + model Condenser "Extension of Condenser with Raoult's Law" + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "This is a non-executable model is created inside the package Distillation to extend the Condenser model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the DistColumn model to create a complete distillation column model which will be instantiated in an executable model.
")); + end Condenser; + + model Tray "Extension of Trays with Raoult's Law" + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "This is a non-executable model is created inside the package Distillation to extend the Tray model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the DistColumn model to create a complete distillation column model which will be instantiated in an executable model.
")); + end Tray; + + model Reboiler "Extension of Reboiler with Raoult's Law" + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "This is a non-executable model is created inside the package Distillation to extend the Reboiler model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the DistColumn model to create a complete distillation column model which will be instantiated in an executable model.
")); + end Reboiler; + + model DistColumn "Extension of Distillation Column along with instances of Condenser, Tray and Reboiler" + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condenser condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + annotation( + Documentation(info = "This is a non-executable model is created inside the package Distillation to extend the Distillation Column model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

Condenser, Tray and Reboiler models are also instantiated in this model to complete building of distillation column model.

It will be instantiated in the DistillationSimulation_Ex1, 
DistillationSimulation_Ex2, DistillationSimulation_Ex3, 
DistillationSimulation_Ex4, DistillationSimulation_Ex5 model to create the required instance of the distillation column model.
")); + end DistColumn; + +model flowsheet +parameter Integer Nc=4; +import data=Simulator.Files.ChemsepDatabase; +parameter data.Propane pro; +parameter data.Isobutane ibut; +parameter data.Nbutane nbut; +parameter data.Isopentane ipen; +parameter data.GeneralProperties C[Nc] = {pro, ibut, nbut, ipen}; + +Isomerisation.MS S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-78, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Isomerisation.DistColumn sdc1(C = C, Ctype = "Total", InT_s = {30}, NQ = 0, Nc = Nc, Ni = 1, Nout = 0, Nt = 62) annotation( + Placement(visible = true, transformation(origin = {-4, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Isomerisation.MS S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {66, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Isomerisation.MS S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {66, -20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S1.P = 101325; + S1.T = 298.157; + S1.F_p[1] = 12.6; + S1.x_pc[1, :] = {0.01, 0.2, 0.74, 0.05}; + + sdc1.condenser.P = 101325; + sdc1.reboiler.P = 101325; + sdc1.RR = 9.00; + S3.x_pc[1, 2] = 0.99000; + connect(S1.Out, sdc1.In_s[1]) annotation( + Line(points = {{-68, 10}, {-29, 10}}, color = {0, 70, 70})); + connect(sdc1.Bot, S3.In) annotation( + Line(points = {{21, -20}, {56, -20}}, color = {0, 70, 70})); + connect(sdc1.Dist, S2.In) annotation( + Line(points = {{21, 40}, {56, 40}}, color = {0, 70, 70})); +end flowsheet; +end Isomerisation; diff --git a/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Abstract.pdf b/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Methanol_Water_Sep.mo b/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Methanol_Water_Sep.mo old mode 100755 new mode 100644 diff --git a/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/README.txt b/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Methanol_Water_Distillation_By_Mr_Rahul_A_S/Methanol_Water.pdf b/Methanol_Water_Distillation_By_Mr_Rahul_A_S/Methanol_Water.pdf old mode 100755 new mode 100644 diff --git a/Methanol_Water_Distillation_By_Mr_Rahul_A_S/Methanol_Water_Distillation.mo b/Methanol_Water_Distillation_By_Mr_Rahul_A_S/Methanol_Water_Distillation.mo old mode 100755 new mode 100644 diff --git a/Methanol_Water_Distillation_By_Mr_Rahul_A_S/README.txt b/Methanol_Water_Distillation_By_Mr_Rahul_A_S/README.txt old mode 100755 new mode 100644 diff --git a/Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/MethanolWaterDistillatioWithPreheating.pdf b/Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/MethanolWaterDistillatioWithPreheating.pdf old mode 100755 new mode 100644 diff --git a/Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/MethanolWaterDistillationWithPreheating.mo b/Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/MethanolWaterDistillationWithPreheating.mo old mode 100755 new mode 100644 diff --git a/Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/README.txt b/Methanol_Water_Distillation_With_Preheating_By_Mr_Deepanshu_Kishnani/README.txt old mode 100755 new mode 100644 diff --git a/Methyl_Acetate_Process_Using_Carbonylation_Of_Dimethyl_Ether_Produced_From_Methanol_By_Ms_Trisha_Dutta/Abstract_Carbonylation_of_DME.pdf b/Methyl_Acetate_Process_Using_Carbonylation_Of_Dimethyl_Ether_Produced_From_Methanol_By_Ms_Trisha_Dutta/Abstract_Carbonylation_of_DME.pdf old mode 100755 new mode 100644 diff --git a/Methyl_Acetate_Process_Using_Carbonylation_Of_Dimethyl_Ether_Produced_From_Methanol_By_Ms_Trisha_Dutta/Carbonylation_of_DME.mo b/Methyl_Acetate_Process_Using_Carbonylation_Of_Dimethyl_Ether_Produced_From_Methanol_By_Ms_Trisha_Dutta/Carbonylation_of_DME.mo old mode 100755 new mode 100644 diff --git a/Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/Nitrogen_Liquefaction.mo b/Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/Nitrogen_Liquefaction.mo old mode 100755 new mode 100644 diff --git a/Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/Nitrogen_Liquefaction_Linde_Cycle.pdf b/Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/Nitrogen_Liquefaction_Linde_Cycle.pdf old mode 100755 new mode 100644 diff --git a/Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/README.txt b/Nitrogen_Liquefaction_Using_Linde_Cycle_By_Mr_Abhishek_Kumar/README.txt old mode 100755 new mode 100644 diff --git a/Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/Abstract.pdf b/Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/README.txt b/Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/openloopturbine.mo b/Open_Cycle_Steam_Turbine_By_Mr_Malapati_Sree_Harsha/openloopturbine.mo old mode 100755 new mode 100644 diff --git a/Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Abstract_Separation_of_methanol_and_diethylamine.pdf b/Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Abstract_Separation_of_methanol_and_diethylamine.pdf new file mode 100644 index 0000000..1a381fa Binary files /dev/null and b/Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Abstract_Separation_of_methanol_and_diethylamine.pdf differ diff --git a/Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Separation_of_Diethylamine_and_Methanol.mo b/Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Separation_of_Diethylamine_and_Methanol.mo new file mode 100644 index 0000000..5277385 --- /dev/null +++ b/Pressure-Swing_Distillation_Process_For_Separation_Of_The_Maximum-Boiling_Azeotrope_Diethylamine_And_Methanol_By_Mr_Eliazer/Separation_of_Diethylamine_and_Methanol.mo @@ -0,0 +1,109 @@ +package Separation_of_Diethylamine_and_Methanol + model matstream + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end matstream; + + model Condensor + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Condensor; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Reboiler; + + model Discolumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end Discolumn; + + model flowsheet + import data = Simulator.Files.ChemsepDatabase; + + parameter data.Methanol meth; + + parameter data.Diethylamine dea; + + parameter Integer Nc = 2; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {meth,dea}; + + Separation_of_Diethylamine_and_Methanol.Discolumn discol1(Nc = Nc, C = C, Nt = 30, Ni = 2, InT_s = {16,22}) annotation( + Placement(visible = true, transformation(origin = {-52, 12}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.matstream feed(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-134, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.matstream d1(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {6, 46}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.matstream b1(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {4, -6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream reb1 annotation( + Placement(visible = true, transformation(origin = {4, -48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream con1 annotation( + Placement(visible = true, transformation(origin = {6, 90}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.matstream d2(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {128, 46}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.matstream b2(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {130, -16}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.Discolumn discol2(Nc = Nc, C = C, Nt = 30, Ni = 1, InT_s = {19}) annotation( + Placement(visible = true, transformation(origin = {62, 12}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream con2 annotation( + Placement(visible = true, transformation(origin = {120, 88}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream reb2 annotation( + Placement(visible = true, transformation(origin = {108, -58}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Separation_of_Diethylamine_and_Methanol.matstream recycle(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-134, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + connect(reb2.Out, discol2.Rduty) annotation( + Line(points = {{118, -58}, {87, -58}, {87, -48}}, color = {255, 0, 0})); + connect(discol2.Cduty, con2.In) annotation( + Line(points = {{87, 72}, {98.5, 72}, {98.5, 88}, {110, 88}}, color = {255, 0, 0})); + connect(discol2.Bot, b2.In) annotation( + Line(points = {{87, -18}, {103.5, -18}, {103.5, -16}, {120, -16}}, color = {0, 70, 70})); + connect(discol2.Dist, d2.In) annotation( + Line(points = {{87, 42}, {102.5, 42}, {102.5, 46}, {118, 46}}, color = {0, 70, 70})); + connect(b1.Out, discol2.In_s[1]) annotation( + Line(points = {{14, -6}, {28, -6}, {28, 12}, {37, 12}}, color = {0, 70, 70})); + connect(feed.Out, discol1.In_s[1]) annotation( + Line(points = {{-124, 18}, {-78, 18}, {-78, 12}, {-77, 12}}, color = {0, 70, 70})); + connect(discol1.Bot, b1.In) annotation( + Line(points = {{-27, -18}, {-15.5, -18}, {-15.5, -6}, {-6, -6}}, color = {0, 70, 70})); + connect(discol1.Rduty, reb1.In) annotation( + Line(points = {{-27, -48}, {-6, -48}}, color = {255, 0, 0})); + connect(discol1.Dist, d1.In) annotation( + Line(points = {{-27, 42}, {-40.25, 42}, {-40.25, 46}, {-4, 46}}, color = {0, 70, 70})); + connect(discol1.Cduty, con1.In) annotation( + Line(points = {{-27, 72}, {-26.5, 72}, {-26.5, 90}, {-4, 90}}, color = {255, 0, 0})); + connect(recycle.Out, discol1.In_s[2]) annotation( + Line(points = {{-124, 4}, {-103.5, 4}, {-103.5, 12}, {-77, 12}}, color = {0, 70, 70})); + + feed.P = 70000; + feed.T = 330; + feed.F_p[1] = 20 ; + feed.x_pc[1, :] = {0.5, 0.5}; + + recycle.P = 70000; + recycle.T = 340; + recycle.F_p[1] = 25; + recycle.x_pc[1, :] = {0.44, 0.56}; + + discol1.condenser.P = 70000; + discol1.reboiler.P = 70000; + discol1.RR = 6; + b1.x_pc[1, 1] = 0.61; + discol2.condenser.P = 202650; + discol2.reboiler.P = 202650; + d2.x_pc[1, 2] = 0.005; + b2.x_pc[1, 1] = 0.46; + + + + end flowsheet; +end Separation_of_Diethylamine_and_Methanol; diff --git a/Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/PSD.mo b/Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/PSD.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/README.txt b/Pressure_Swing_Azeotropic_Distillation_Of_Methanol_And_Acetone_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Abstract_PSDMeth.pdf b/Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Abstract_PSDMeth.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Flowsheet_PSDMeth.mo b/Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/Flowsheet_PSDMeth.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/README.txt b/Pressure_Swing_Distillation_For_Methanol_-_Chloroform_Separation_By_Mr_Gaurav_Tiwari/README.txt old mode 100755 new mode 100644 diff --git "a/Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/Abstract.pdf" "b/Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/Abstract.pdf" old mode 100755 new mode 100644 diff --git "a/Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/PSD_EA_EO.mo" "b/Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/PSD_EA_EO.mo" old mode 100755 new mode 100644 diff --git "a/Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/README.txt" "b/Pressure_Swing_Distillation_For_Separating_A_Minimum_Boiling_Azeotrope_Of_Ethyl_Acetate_And_Ethanol\t_By_Mr_Neel_Pulin_Modi/README.txt" old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Abstract_Separation_Of_Ethyl_Acetate_And_Cyclohexane_using_PSD.pdf b/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Abstract_Separation_Of_Ethyl_Acetate_And_Cyclohexane_using_PSD.pdf new file mode 100644 index 0000000..d9f12f6 Binary files /dev/null and b/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Abstract_Separation_Of_Ethyl_Acetate_And_Cyclohexane_using_PSD.pdf differ diff --git a/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Flowsheet_PSD.mo b/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Flowsheet_PSD.mo new file mode 100644 index 0000000..0ed33f1 --- /dev/null +++ b/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/Flowsheet_PSD.mo @@ -0,0 +1,120 @@ +package Flowsheet_PSD + model MS + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end MS; + + model Compressor + extends Simulator.UnitOperations.AdiabaticCompressor; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Compressor; + + model Flowsheet "Pressure Swing Distillation For Separation Of Ethyl Acetate And Cyclohexane" + import data = Simulator.Files.ChemsepDatabase; + parameter data.Ethylacetate Ethac; + parameter data.Cyclohexane Cyclo; + parameter Integer Nc = 2; + parameter data.GeneralProperties C[Nc] = {Ethac, Cyclo}; + //....................................................................... + Flowsheet_PSD.MS Feed(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-248, -26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS Recycle(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-248, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.PCPack.PC HPC1(C = C, Ctype = "Total", InT_s = {2, 11}, Nc = Nc, Ni = 2, Nt = 34) annotation( + Placement(visible = true, transformation(origin = {-142, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-78, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS Distillate1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-78, -36}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.Compressor C1(C = C, Eff = 1, F_p(start = {38.78, 15.2461, 23.5339}), Nc = Nc, T(start = 330.532), x_pc(start = {{0.891354, 0.108646}, {0.887739, 0.112261}, {0.893695, 0.106305}})) annotation( + Placement(visible = true, transformation(origin = {-32, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS S2(C = C, F_p(start = {38.8435, 15.2716, 23.5719}), H_p(start = {-9307.4, -29513.6, 3783.69}), Nc = Nc, T(start = 330.532), x_pc(start = {{0.891531, 0.108469}, {0.887922, 0.112078}, {0.893869, 0.106131}})) annotation( + Placement(visible = true, transformation(origin = {24, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream En1 annotation( + Placement(visible = true, transformation(origin = {-42, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {162, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS Distillate2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {160, -34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.PCPack.PC LPC2(C = C, Ctype = "Total", InT_s = {28}, Nc = Nc, Ni = 1, Nt = 35) annotation( + Placement(visible = true, transformation(origin = {100, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve V1(C = C, Fin(start = 25.2172), Nc = Nc, Tin(start = 330.92)) annotation( + Placement(visible = true, transformation(origin = {210, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Flowsheet_PSD.MS To_Recycle(C = C, F_p(start = {25.2172, 25.2172, 0}), H_p(start = {-29390.6, -29390.6, 0}), Nc = Nc, T(start = 330.92), x_pc(start = {{0.864819, 0.135181}, {0.864819, 0.135181}, {0, 0}})) annotation( + Placement(visible = true, transformation(origin = {264, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + connect(Recycle.Out, HPC1.In_s[1]) annotation( + Line(points = {{-238, 32}, {-192, 32}, {-192, 4}, {-167, 4}}, color = {0, 70, 70})); + connect(Feed.Out, HPC1.In_s[2]) annotation( + Line(points = {{-238, -26}, {-192, -26}, {-192, 4}, {-167, 4}}, color = {0, 70, 70})); + connect(HPC1.Dist, S1.In) annotation( + Line(points = {{-117, 34}, {-117, 37}, {-88, 37}, {-88, 44}}, color = {0, 70, 70})); + connect(HPC1.Bot, Distillate1.In) annotation( + Line(points = {{-117, -26}, {-102.5, -26}, {-102.5, -36}, {-88, -36}}, color = {0, 70, 70})); +//.............................................................. + Feed.P = 1013250; + Feed.T = 303.15; + Feed.x_pc[1, :] = {0.5, 0.5}; + Feed.F_p[1] = 27.7778; + Recycle.P = 1013250; + Recycle.T = 330.429; + Recycle.x_pc[1, :] = {0.83548378, 0.16451622}; + Recycle.F_p[1] = 25.0155; + HPC1.condenser.P = 1013250; + HPC1.reboiler.P = 1013250; + HPC1.RR = 3.66; + Distillate1.F_p[1] = 14.0133; +//Distillate1.x_pc[1, 1] = 0.01; + C1.Pout = 50000; + LPC2.condenser.P = 50662.5; + LPC2.reboiler.P = 0.5; + LPC2.RR = 2.96; + Distillate2.F_p[1] = 13.5628; +//Distillate2.x_pc[1, 1] = 0.999; + V1.Pout = 1013250; +//.................................................................... + connect(S1.Out, C1.In) annotation( + Line(points = {{-68, 44}, {-42, 44}}, color = {0, 70, 70})); + connect(C1.Out, S2.In) annotation( + Line(points = {{-22, 44}, {14, 44}}, color = {0, 70, 70})); + connect(En1.Out, C1.En) annotation( + Line(points = {{-32, 6}, {-32, 37}}, color = {255, 0, 0})); + connect(S2.Out, LPC2.In_s[1]) annotation( + Line(points = {{34, 44}, {56, 44}, {56, 4}, {75, 4}}, color = {0, 70, 70})); + connect(LPC2.Dist, S3.In) annotation( + Line(points = {{125, 34}, {152, 34}, {152, 38}}, color = {0, 70, 70})); + connect(LPC2.Bot, Distillate2.In) annotation( + Line(points = {{125, -26}, {150, -26}, {150, -34}}, color = {0, 70, 70})); + connect(V1.In, S3.Out) annotation( + Line(points = {{200, 38}, {172, 38}}, color = {0, 70, 70})); + connect(V1.Out, To_Recycle.In) annotation( + Line(points = {{220, 38}, {254, 38}}, color = {0, 70, 70})); + annotation( + Diagram(coordinateSystem(extent = {{-300, -100}, {300, 100}})), + Icon(coordinateSystem(extent = {{-300, -100}, {300, 100}}))); + end Flowsheet; + + package PCPack + model Condenser + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Condenser; + + model PC + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condenser condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end PC; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Reboiler; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Tray; + end PCPack; +end Flowsheet_PSD; diff --git a/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/README.txt b/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/README.txt new file mode 100644 index 0000000..1c179b6 --- /dev/null +++ b/Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate_And_Cyclohexane_By_Mr_Sayyed_Sohel_Mujammil/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Pressure Swing Distillation for Separation of Ethyl Acetate and Cyclohexane +Proposar Name: Mr Sayyed Sohel Mujammil +University: Vishwakarma Institute of Technology, Pune-411048 + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/Abstract.pdf b/Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/Flowsheet_PSDMethanol.mo b/Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/Flowsheet_PSDMethanol.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/README.txt b/Pressure_Swing_Distillation_For_Separation_Of_Tetrahydrofuran-Methanol_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/PSDwithRecycle.mo b/Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/PSDwithRecycle.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/README.txt b/Pressure_Swing_Distillation_Of_Acetonitrile-Water_System_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Abstract.pdf b/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Flowsheet_PSDWater.mo b/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Flowsheet_PSDWater.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/README.txt b/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/Flowsheet_PSDEthyl.mo b/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/Flowsheet_PSDEthyl.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/README.txt b/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/abstract.pdf b/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Abstract.pdf b/Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Flowsheet_PSDIsobutanol.mo b/Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/Flowsheet_PSDIsobutanol.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/README.txt b/Pressure_Swing_Distillation_Of_Isobutanol_And_N-Heptane_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/Abstract_PSD_Toluene_Ethanol.pdf b/Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/Abstract_PSD_Toluene_Ethanol.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/PSD.mo b/Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/PSD.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/README.txt b/Pressure_Swing_Distillation_Of_Toluene_And_Ethanol_By_Mr_Kaushik_Datta/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/PSD_Abstract.pdf b/Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/PSD_Abstract.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/PresSwingDist.mo b/Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/PresSwingDist.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/README.txt b/Pressure_Swing_Distillation_System_For_Methylal_methanol_By_Mr_Sandeep_Kumar_Samanta/README.txt old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/Abstract_PSD.pdf b/Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/Abstract_PSD.pdf old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/Flowsheet_PSD.mo b/Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/Flowsheet_PSD.mo old mode 100755 new mode 100644 diff --git a/Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/README.txt b/Pressure_Swing_Distillation_To_Separate_Isobutyl_Acetate_And_Isobutyl_Alcohol_By_Mr_Akshay_Kumar_Mehta/README.txt old mode 100755 new mode 100644 diff --git a/Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/OpenModelica_Flowsheeting_Project_Abstract_v01_31Oct2019.pdf b/Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/OpenModelica_Flowsheeting_Project_Abstract_v01_31Oct2019.pdf old mode 100755 new mode 100644 diff --git a/Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/Process_Development_for_the_Production_of_Propylene_Oxide.mo b/Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/Process_Development_for_the_Production_of_Propylene_Oxide.mo old mode 100755 new mode 100644 diff --git a/Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/README.txt b/Process_Development_For_The_Production_Of_Propylene_Oxide_By_Mr_Jayaram_Ganesan/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Abstract.pdf b/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Abstract.pdf new file mode 100644 index 0000000..ccada18 Binary files /dev/null and b/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Abstract.pdf differ diff --git a/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Ethylbenzene.mo b/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Ethylbenzene.mo new file mode 100644 index 0000000..8af7881 --- /dev/null +++ b/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/Ethylbenzene.mo @@ -0,0 +1,204 @@ +package Ethylbenzene + model flowsheet + extends Modelica.Icons.Example; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Benzene ben; + parameter data.Ethylene ethe; + parameter data.Ethylbenzene ethlben; + parameter Integer Nc = 3; + parameter data.GeneralProperties C[Nc] = {ben,ethe,ethlben}; + Ethylbenzene.ms S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-269, 85}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer1(C = C, NI =2, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-241, 85}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.ms S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-214, 83}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Simulator.Streams.EnergyStream E01 annotation( + Placement(visible = true, transformation(origin = {-214, 62}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-160, 83}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.conv_react conv_react1(BC_r = {2}, C = C, CalcMode = "Define_Out_Temperature",Coef_cr = {{-1}, {-1}, {1}}, Nc = Nc, Nr = 1, Tdef = 483.15, X_r = {0.9}) annotation( + Placement(visible = true, transformation(origin = {-191, 81}, extent = {{-7, -7}, {7, 7}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-133, 83}, extent = {{-7, -7}, {7, 7}}, rotation = 0))); + Simulator.Streams.EnergyStream E02 annotation( + Placement(visible = true, transformation(origin = {-116, 66}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-108, 83}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.Shortcut shortcut1(C = C, Ctype = "Total", HKey = 3, LKey = 2, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-77, 73}, extent = {{-5, -5}, {5, 5}}, rotation = 0))); + Simulator.Streams.EnergyStream E03 annotation( + Placement(visible = true, transformation(origin = {-50, 102}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E04 annotation( + Placement(visible = true, transformation(origin = {-74, 34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-48, 89}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.ms S6(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-50, 59}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler2(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-26, 60}, extent = {{-6, -6}, {6, 6}}, rotation = 0))); + Simulator.Streams.EnergyStream E05 annotation( + Placement(visible = true, transformation(origin = {-11, 47}, extent = {{-7, -7}, {7, 7}}, rotation = 0))); + Ethylbenzene.ms S7(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-4, 61}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.Shortcut shortcut2(C = C, Ctype = "Total", HKey = 3, LKey = 2, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {29, 61}, extent = {{-5, -5}, {5, 5}}, rotation = 0))); + Simulator.Streams.EnergyStream E06 annotation( + Placement(visible = true, transformation(origin = {32, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E07 annotation( + Placement(visible = true, transformation(origin = {60, 90}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S8(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {58, 77}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.ms S9(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {58, 45}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler3(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {84, 46}, extent = {{-6, -6}, {6, 6}}, rotation = 0))); + Simulator.Streams.EnergyStream E08 annotation( + Placement(visible = true, transformation(origin = {98, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S10(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {110, 45}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.Shortcut shortcut3(C = C, Ctype = "Total", HKey = 3, LKey = 2, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {142, 46}, extent = {{-4, -4}, {4, 4}}, rotation = 0))); + Simulator.Streams.EnergyStream E09 annotation( + Placement(visible = true, transformation(origin = {150, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E10 annotation( + Placement(visible = true, transformation(origin = {172, 74}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S11(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {178, 57}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.ms S12(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {178, 29}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Ethylbenzene.ms recycle(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-268, 75}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer2(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {214, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S13(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {246, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms S14(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {300, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater heater1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {274, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E11 annotation( + Placement(visible = true, transformation(origin = {248, 52}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve valve1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {330, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Ethylbenzene.ms Recycle(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {364, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S1.P = 2000000; + S1.T = 483.15; + S1.x_pc[1, :] = {0.5, 0.5, 0}; + S1.F_p[1] = 319.444; + recycle.P = 2000000; + recycle.T = 513.348; + recycle.x_pc[1, :] = {0.051544408, 0.4165792, 0.53219767}; + recycle.F_p[1] = 35.1762; + S4.T = 423.15; + shortcut1.Preb = 1.5E6; + shortcut1.Pcond = 1.5E6; + shortcut1.x_pc[2, shortcut1.LKey] = 0.07539; + shortcut1.x_pc[3, shortcut1.HKey] = 0.1148; + shortcut1.RR = 1.5; + S7.T = 407.15; + shortcut2.Preb = 200000; + shortcut2.Pcond = 200000; + shortcut2.x_pc[2, shortcut1.LKey] = 0.00611; + shortcut2.x_pc[3, shortcut1.HKey] = 0.4758; + shortcut2.RR = 1.5; + S10.T = 334.78; + shortcut3.Preb = 0.1E5; + shortcut3.Pcond = 0.1E5; + shortcut3.x_pc[2, shortcut1.LKey] = 0.00015; + shortcut3.x_pc[3, shortcut1.HKey] = 0.7613; + shortcut3.RR = 1.5; + S14.T=483.15; + valve1.Pout=2000000; + connect(S1.Out, mixer1.In[1]) annotation( + Line(points = {{-260, 85}, {-250, 85}}, color = {0, 70, 70})); + connect(mixer1.Out, S2.In) annotation( + Line(points = {{-232, 86}, {-223, 86}, {-223, 83}}, color = {0, 70, 70})); + connect(E01.Out, conv_react1.energy) annotation( + Line(points = {{-204, 62}, {-191, 62}, {-191, 72}}, color = {255, 0, 0})); + connect(S2.Out, conv_react1.In) annotation( + Line(points = {{-204, 84}, {-201, 84}, {-201, 81}, {-198, 81}}, color = {0, 70, 70})); + connect(conv_react1.Out, S3.In) annotation( + Line(points = {{-184, 81}, {-173, 81}, {-173, 84}, {-168, 84}}, color = {0, 70, 70})); + connect(cooler1.En, E02.In) annotation( + Line(points = {{-126, 76}, {-126, 76}, {-126, 66}, {-126, 66}}, color = {255, 0, 0})); + connect(S3.Out, cooler1.In) annotation( + Line(points = {{-150, 84}, {-140, 84}, {-140, 84}, {-140, 84}}, color = {0, 70, 70})); + connect(cooler1.Out, S4.In) annotation( + Line(points = {{-126, 84}, {-118, 84}, {-118, 84}, {-116, 84}}, color = {0, 70, 70})); + connect(S4.Out, shortcut1.In) annotation( + Line(points = {{-98, 84}, {-89.5, 84}, {-89.5, 73}}, color = {0, 70, 70})); + connect(E04.Out, shortcut1.En2) annotation( + Line(points = {{-64, 34}, {-64, 34}, {-64, 44}, {-64, 44}}, color = {255, 0, 0})); + connect(shortcut1.En1, E03.In) annotation( + Line(points = {{-64, 104}, {-60, 104}, {-60, 102}, {-60, 102}}, color = {255, 0, 0})); + connect(shortcut1.Out1, S5.In) annotation( + Line(points = {{-64, 88}, {-57, 88}, {-57, 89}}, color = {0, 70, 70})); + connect(shortcut1.Out2, S6.In) annotation( + Line(points = {{-64, 58}, {-59, 58}, {-59, 59}}, color = {0, 70, 70})); + connect(cooler2.En, E05.In) annotation( + Line(points = {{-20, 54}, {-18, 54}, {-18, 48}, {-18, 48}}, color = {255, 0, 0})); + connect(S6.Out, cooler2.In) annotation( + Line(points = {{-40, 60}, {-32, 60}, {-32, 60}, {-32, 60}}, color = {0, 70, 70})); + connect(cooler2.Out, S7.In) annotation( + Line(points = {{-20, 60}, {-12, 60}, {-12, 62}, {-12, 62}}, color = {0, 70, 70})); + connect(E06.Out, shortcut2.En2) annotation( + Line(points = {{42, 20}, {42, 20}, {42, 32}, {42, 32}, {42, 32}}, color = {255, 0, 0})); + connect(shortcut2.En1, E07.In) annotation( + Line(points = {{42, 92}, {50, 92}, {50, 90}, {50, 90}}, color = {255, 0, 0})); + connect(shortcut2.Out1, S8.In) annotation( + Line(points = {{42, 76}, {48, 76}, {48, 78}, {50, 78}}, color = {0, 70, 70})); + connect(shortcut2.Out2, S9.In) annotation( + Line(points = {{42, 46}, {50, 46}, {50, 46}, {50, 46}}, color = {0, 70, 70})); + connect(S7.Out, shortcut2.In) annotation( + Line(points = {{6, 62}, {16, 62}, {16, 62}, {16, 62}, {16, 62}}, color = {0, 70, 70})); + connect(cooler3.En, E08.In) annotation( + Line(points = {{90, 40}, {88, 40}, {88, 32}, {88, 32}}, color = {255, 0, 0})); + connect(S9.Out, cooler3.In) annotation( + Line(points = {{68, 46}, {78, 46}, {78, 46}, {78, 46}}, color = {0, 70, 70})); + connect(cooler3.Out, S10.In) annotation( + Line(points = {{90, 46}, {94, 46}, {94, 45}, {101, 45}}, color = {0, 70, 70})); + connect(S10.Out, shortcut3.In) annotation( + Line(points = {{120, 46}, {132, 46}}, color = {0, 70, 70})); + connect(E09.Out, shortcut3.En2) annotation( + Line(points = {{160, -2}, {160, 4}, {152, 4}, {152, 22}}, color = {255, 0, 0})); + connect(shortcut3.En1, E10.In) annotation( + Line(points = {{152, 70}, {162, 70}, {162, 74}}, color = {255, 0, 0})); + connect(shortcut3.Out2, S12.In) annotation( + Line(points = {{152, 34}, {162.75, 34}, {162.75, 30}, {170, 30}}, color = {0, 70, 70})); + connect(shortcut3.Out1, S11.In) annotation( + Line(points = {{152, 58}, {166, 58}, {166, 57}, {169, 57}}, color = {0, 70, 70})); + connect(recycle.Out, mixer1.In[2]) annotation( + Line(points = {{-258, 76}, {-250, 76}, {-250, 86}, {-250, 86}}, color = {0, 70, 70})); + connect(S8.Out, mixer2.In[1]) annotation( + Line(points = {{68, 78}, {204, 78}, {204, 68}, {204, 68}}, color = {0, 70, 70})); + connect(S11.Out, mixer2.In[2]) annotation( + Line(points = {{188, 58}, {204, 58}, {204, 68}, {204, 68}}, color = {0, 70, 70})); + connect(mixer2.Out, S13.In) annotation( + Line(points = {{224, 68}, {236, 68}, {236, 68}, {236, 68}}, color = {0, 70, 70})); + connect(S13.Out, heater1.In) annotation( + Line(points = {{256, 68}, {264, 68}, {264, 68}, {264, 68}}, color = {0, 70, 70})); + connect(E11.Out, heater1.En) annotation( + Line(points = {{258, 52}, {264, 52}, {264, 58}, {264, 58}}, color = {255, 0, 0})); + connect(heater1.Out, S14.In) annotation( + Line(points = {{284, 68}, {290, 68}, {290, 68}, {290, 68}}, color = {0, 70, 70})); + connect(S14.Out, valve1.In) annotation( + Line(points = {{310, 68}, {320, 68}, {320, 68}, {320, 68}}, color = {0, 70, 70})); + connect(valve1.Out, Recycle.In) annotation( + Line(points = {{340, 68}, {354, 68}, {354, 68}, {354, 68}}, color = {0, 70, 70})); + end flowsheet; +model ms + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end ms; +model conv_react + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; +end conv_react; +model Shortcut +extends Simulator.UnitOperations.ShortcutColumn; +extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end Shortcut; +end Ethylbenzene; diff --git a/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/README.txt b/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/README.txt new file mode 100644 index 0000000..0e4ab28 --- /dev/null +++ b/Production_Of_1400_Tpd_Of_Ethylbenzene_By_Liquid_Phase_Alkylation_Of_Benzene_By_Mr_Aniruddh_Mukunth/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Production of 1400 TPD of Ethylbenzene by Liquid Phase Alkylation of Benzene +Proposar Name: Mr Aniruddh Mukunth +University: SASTRA Deemed to be University + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/AceticAcidAbstract.pdf b/Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/AceticAcidAbstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/README.txt b/Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/aceticacid.mo b/Production_Of_Acetic_Acid_By_Mr_Malapati_Sree_Harsha/aceticacid.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid.mo b/Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid_Abstract.pdf b/Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/Aceticacid_Abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/README.txt b/Production_Of_Acetic_Acid_Using_Acetaldehyde_By_Mr_Sandeep_Kumar_Samanta/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/Ammonia.mo b/Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/Ammonia.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/AmmoniaAbs.pdf b/Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/AmmoniaAbs.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/README.txt b/Production_Of_Ammonia_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/README.txt b/Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/ammonia.pdf b/Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/ammonia.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/ammonia_by_haber_new.mo b/Production_Of_Ammonia_Through_Haber'S_Process_By_Mr_Mehulkumar_Sutariya/ammonia_by_haber_new.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/Abstract_ButanalProduction.pdf b/Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/Abstract_ButanalProduction.pdf new file mode 100644 index 0000000..f05f4c4 Binary files /dev/null and b/Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/Abstract_ButanalProduction.pdf differ diff --git a/Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/butanal.mo b/Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/butanal.mo new file mode 100644 index 0000000..c374083 --- /dev/null +++ b/Production_Of_Butanal_From_Propylene,_Carbon_Monoxide_And_Hydrogen_Using_Recycle_Stream_By_Mr_Swetank_Sahai/butanal.mo @@ -0,0 +1,148 @@ +package butanal + + model mat + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end mat; + + model convreactor + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; + end convreactor; + + model sep + extends Simulator.UnitOperations.CompoundSeparator; + end sep; + + model FlashSep + extends Simulator.UnitOperations.Flash; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end FlashSep; + + model Flowsheet_ButanalProduction + extends Modelica.Icons.Example; + // Defination of the unit operations and streams used + import data = Simulator.Files.ChemsepDatabase; + + //Number of Components + parameter Integer Nc = 5; + + //Instantiation of compositions + parameter data.Butanal but; + parameter data.Propylene ppy; + parameter data.Propane pro; + parameter data.Carbonmonoxide co; + parameter data.Hydrogen h2; + parameter data.GeneralProperties C[Nc] = {ppy, pro, co, h2, but}; + //Material Streams F1 F2 R + butanal.mat F1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-88, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + butanal.mat F2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-88, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + butanal.mat R(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-88, -4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Mixer M + Simulator.UnitOperations.Mixer M(C = C, NI = 3, Nc = Nc, outPress = "Inlet_Average") annotation( + Placement(visible = true, transformation(origin = {-60, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Material Stream M1 + butanal.mat M1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-36, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Conversion Reactor CR + butanal.convreactor CR(BC_r = {1}, C = C, CalcMode = "Isothermal", Coef_cr = {{-1}, {0}, {-1}, {-1}, {1}}, Nc = Nc, Nr = 1, X_r = fill(0.9, 1)) annotation( + Placement(visible = true, transformation(origin = {-12, 10}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + + //Material Stream M2 + butanal.mat M2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {12, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Compound Separator SR + butanal.sep SR(C = C, Nc = Nc, SepFact_c = {"Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent"}, SepStrm = 1) annotation( + Placement(visible = true, transformation(origin = {38, 10}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + + //Material Stream M3 M4 + butanal.mat M3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {62, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + butanal.mat M4(C = C, Fg = 50, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {62, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Energy Stream E1 E2 + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-22, -26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {28, -26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Compound Separator SR2 + butanal.sep SR2(C = C, Nc = Nc, SepFact_c = {"Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent"}, SepStrm = 1) annotation( + Placement(visible = true, transformation(origin = {84, -36}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + + //Material Stream M5 M6 + butanal.mat M5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {114, -44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + mat M6(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {114, -28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + //Energy Stream E3 + Simulator.Streams.EnergyStream E3 annotation( + Placement(visible = true, transformation(origin = {74, -76}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + + equation + connect(F1.Out, M.In[1]) annotation( + Line(points = {{-78, 22}, {-74, 22}, {-74, 10}, {-70, 10}}, color = {0, 70, 70})); + connect(F2.Out, M.In[2]) annotation( + Line(points = {{-78, 10}, {-70, 10}}, color = {0, 70, 70})); + connect(R.Out, M.In[3]) annotation( + Line(points = {{-78, -4}, {-74, -4}, {-74, 10}, {-70, 10}}, color = {0, 70, 70})); + connect(M1.In, M.Out) annotation( + Line(points = {{-46, 10}, {-50, 10}}, color = {0, 70, 70})); + connect(M1.Out, CR.In) annotation( + Line(points = {{-26, 10}, {-22, 10}}, color = {0, 70, 70})); + connect(M2.In, CR.Out) annotation( + Line(points = {{2, 10}, {-2, 10}}, color = {0, 70, 70})); + connect(SR.In, M2.Out) annotation( + Line(points = {{28, 10}, {22, 10}}, color = {0, 70, 70})); + connect(M3.In, SR.Out2) annotation( + Line(points = {{52, 2}, {48, 2}}, color = {0, 70, 70})); + connect(M4.In, SR.Out1) annotation( + Line(points = {{52, 18}, {48, 18}}, color = {0, 70, 70})); + + //Feed F1 + F1.F_p[1] = 50; + F1.x_pc[1, :] = {0.95, 0.05, 0, 0, 0}; + F1.P = 101325; + F1.T = 300; + + //Feed F2 + F2.F_p[1] = 120; + F2.x_pc[1, :] = {0, 0, 0.5, 0.5, 0}; + F2.P = 101325; + F2.T = 300; + + //Recycle R + R.F_p[1] = 3.4; + R.x_pc[1, :] = {0.55, 0.45, 0, 0, 0}; + R.P = 101325; + R.T = 300; + + //Assigning Separation Criterion + + SR.SepVal_c = {0, 0, 0, 0, 100}; + SR2.SepVal_c = {0, 0, 100, 100, 0}; + + connect(E1.Out, CR.energy) annotation( + Line(points = {{-12, -26}, {-12, -2}}, color = {255, 0, 0})); + connect(E2.Out, SR.En) annotation( + Line(points = {{38, -26}, {38, -2}}, color = {255, 0, 0})); + connect(M3.Out, SR2.In) annotation( + Line(points = {{72, 2}, {72, -36}, {74, -36}}, color = {0, 70, 70})); + connect(M6.In, SR2.Out1) annotation( + Line(points = {{104, -28}, {94, -28}}, color = {0, 70, 70})); + connect(M5.In, SR2.Out2) annotation( + Line(points = {{104, -44}, {94, -44}}, color = {0, 70, 70})); + connect(E3.Out, SR2.En) annotation( + Line(points = {{84, -76}, {84, -48}}, color = {255, 0, 0})); + end Flowsheet_ButanalProduction; + +end butanal; diff --git a/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Chlorobenzene.mo b/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Chlorobenzene.mo new file mode 100644 index 0000000..bb4992a --- /dev/null +++ b/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Chlorobenzene.mo @@ -0,0 +1,166 @@ +package Chlorobenzene +model flowsheet +extends Modelica.Icons.Example; +import data = Simulator.Files.ChemsepDatabase; +parameter data.Benzene ben; +parameter data.Chlorine chlo; +parameter data.Monochlorobenzene chben; +parameter data.Hydrogenchloride hcl; +parameter data.Odichlorobenzene Ochben; +parameter data.Pdichlorobenzene Pchben; +parameter Integer Nc = 6; +parameter data.GeneralProperties C[Nc] = {ben,chlo,chben,hcl,Ochben,Pchben}; +Chlorobenzene.ms S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-222, 46}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); +Chlorobenzene.ms S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-222, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); +Chlorobenzene.ms S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-222, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer1(C = C, NI = 3, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-182, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-152, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-82, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.conv_react CR(BC_r = {1,1,1}, C = C, CalcMode = "Isothermal", Coef_cr = {{-1, -1,-1}, {-1, -2,-2}, {1, 0,0}, {1, 2,2}, {0, 1,0}, {0, 0,1}},Nc = Nc, Nr = 3, X_r = {0.719, 0.0448314,0.0768454}) annotation( + Placement(visible = true, transformation(origin = {-56, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S6(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-24, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E01 annotation( + Placement(visible = true, transformation(origin = {-144, 12}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater heater1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-118, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E02 annotation( + Placement(visible = true, transformation(origin = {-70, -6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.CompoundSeparator CS1(C = C, Nc = Nc, SepFact_c = { "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent","Inlet_Molar_Flow_Percent","Inlet_Molar_Flow_Percent","Inlet_Molar_Flow_Percent"}, SepStrm = 2) annotation( + Placement(visible = true, transformation(origin = {8, 26}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Simulator.Streams.EnergyStream E03 annotation( + Placement(visible = true, transformation(origin = {20, -10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S7(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {42, 34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S8(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = { 42, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.DistColumn distColumn1(C = C, Ctype = "Total", InT_s = {3}, Nc = Nc, Ni = 1, Nt = 12) annotation( + Placement(visible = true, transformation(origin = {92, 34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E4 annotation( + Placement(visible = true, transformation(origin = {108, -36}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E5 annotation( + Placement(visible = true, transformation(origin = {136, 94}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S9(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {146, 64}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S10(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {144, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.DistColumn distColumn2(C = C, Ctype = "Total", InT_s = {5}, Nc = Nc, Ni = 1, Nt = 7) annotation( + Placement(visible = true, transformation(origin = {196, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E6 annotation( + Placement(visible = true, transformation(origin = {246, 66}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E7 annotation( + Placement(visible = true, transformation(origin = {212, -62}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S11(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {244, 36}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Chlorobenzene.ms S12(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {244, -24}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); +equation + connect(distColumn2.Dist, S11.In) annotation( + Line(points = {{222, 36}, {234, 36}, {234, 36}, {234, 36}}, color = {0, 70, 70})); + connect(distColumn2.Bot, S12.In) annotation( + Line(points = {{222, -24}, {234, -24}, {234, -24}, {234, -24}}, color = {0, 70, 70})); + connect(distColumn2.Cduty, E6.In) annotation( + Line(points = {{222, 66}, {236, 66}, {236, 66}, {236, 66}}, color = {255, 0, 0})); + connect(E7.Out, distColumn2.Rduty) annotation( + Line(points = {{222, -62}, {220, -62}, {220, -54}, {222, -54}}, color = {255, 0, 0})); + connect(S10.Out, distColumn2.In_s[1]) annotation( + Line(points = {{154, 6}, {170, 6}, {170, 6}, {172, 6}}, color = {0, 70, 70})); + connect(distColumn1.Cduty, E5.In) annotation( + Line(points = {{118, 94}, {126, 94}, {126, 94}, {126, 94}}, color = {255, 0, 0})); + connect(E4.Out, distColumn1.Rduty) annotation( + Line(points = {{118, -36}, {116, -36}, {116, -26}, {118, -26}}, color = {255, 0, 0})); + connect(distColumn1.Bot, S10.In) annotation( + Line(points = {{118, 4}, {134, 4}, {134, 6}, {134, 6}}, color = {0, 70, 70})); + connect(distColumn1.Dist, S9.In) annotation( + Line(points = {{118, 64}, {134, 64}, {134, 64}, {136, 64}, {136, 64}}, color = {0, 70, 70})); + connect(S7.Out, distColumn1.In_s[1]) annotation( + Line(points = {{52, 34}, {66, 34}, {66, 34}, {68, 34}}, color = {0, 70, 70})); + connect(CS1.Out1, S7.In) annotation( + Line(points = {{18, 34}, {32, 34}}, color = {0, 70, 70})); + S1.P = 101325; + S1.T = 313.15; + S1.F_p[1] = 12.8022; + S1.x_pc[1, :] = {1, 0, 0, 0, 0, 0}; + S2.P = 101325; + S2.T = 313.15; + S2.F_p[1] = 14.1032; + S2.x_pc[1, :] = {0, 1, 0, 0, 0, 0}; + S3.P = 101325; + S3.T = 357.921; + S3.F_p[1] = 2.23642; + S3.x_pc[1, :] = {0.82265932,0,0.17683247,2.5989955E-19,0.00013811427,0.00037009984}; + S5.T = 313.5; + CS1.SepVal_c = {0, 100, 0, 100, 0, 0}; + distColumn1.condenser.P=101325; + distColumn1.reboiler.P=111325; + distColumn1.RR=1.205; + S10.F_p[1] = 11.94; + distColumn2.condenser.P=101325; + distColumn2.reboiler.P=111325; + distColumn2.RR=1.5; + S11.F_p[1] = 10.4546; + connect(S1.Out, mixer1.In[1]) annotation( + Line(points = {{-212, 46}, {-192, 46}, {-192, 26}}, color = {0, 70, 70})); + connect(S2.Out, mixer1.In[2]) annotation( + Line(points = {{-212, 22}, {-192, 22}, {-192, 26}}, color = {0, 70, 70})); + connect(S3.Out, mixer1.In[3]) annotation( + Line(points = {{-212, 4}, {-192, 4}, {-192, 26}}, color = {0, 70, 70})); + connect(mixer1.Out, S4.In) annotation( + Line(points = {{-172, 26}, {-162, 26}}, color = {0, 70, 70})); + connect(S4.Out, heater1.In) annotation( + Line(points = {{-142, 26}, {-128, 26}}, color = {0, 70, 70})); + connect(heater1.Out, S5.In) annotation( + Line(points = {{-108, 26}, {-92, 26}}, color = {0, 70, 70})); + connect(E01.Out, heater1.En) annotation( + Line(points = {{-134, 12}, {-128, 12}, {-128, 16}}, color = {255, 0, 0})); + connect(E02.Out, CR.energy) annotation( + Line(points = {{-60, -6}, {-56, -6}, {-56, 13}}, color = {255, 0, 0})); + connect(S5.Out, CR.In) annotation( + Line(points = {{-72, 26}, {-66, 26}}, color = {0, 70, 70})); + connect(CR.Out, S6.In) annotation( + Line(points = {{-46, 26}, {-34, 26}}, color = {0, 70, 70})); + connect(CS1.En, E03.In) annotation( + Line(points = {{8, 13}, {8, 1.5}, {10, 1.5}, {10, -10}}, color = {255, 0, 0})); + connect(S6.Out, CS1.In) annotation( + Line(points = {{-14, 26}, {-2, 26}}, color = {0, 70, 70})); + connect(CS1.Out2, S8.In) annotation( + Line(points = {{18, 18}, {32, 18}}, color = {0, 70, 70})); + end flowsheet; +model ms + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.NRTL; +end ms; +model conv_react + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; +end conv_react; + + +model Condenser + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Condenser; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Reboiler; + + model DistColumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condenser condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end DistColumn; +end Chlorobenzene; diff --git a/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Production_of_Chlorobenzene.pdf b/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Production_of_Chlorobenzene.pdf new file mode 100644 index 0000000..253c664 Binary files /dev/null and b/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/Production_of_Chlorobenzene.pdf differ diff --git a/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/README.txt b/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/README.txt new file mode 100644 index 0000000..7d20001 --- /dev/null +++ b/Production_Of_Chlorobenzene_From_Benzene_And_Chlorine_By_Mr_Aniruddh_Mukunth/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Production of Chlorobenzene from Benzene and Chlorine +Proposar Name: Mr Aniruddh Mukunth +University: SASTRA Deemed to be University + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/Cumenewithrecycle.mo b/Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/Cumenewithrecycle.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/README.txt b/Production_Of_Cumene_From_Benzene_And_Propylene_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheet.mo b/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheet.mo new file mode 100644 index 0000000..7b3586a --- /dev/null +++ b/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheet.mo @@ -0,0 +1,174 @@ +package CyclohexaneTry2 + model Material + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Material; + + model Mainflow + import data = Simulator.Files.ChemsepDatabase; + parameter data.Nitrogen nit; + parameter data.Hydrogen hy; + parameter data.Cyclohexane ch; + parameter data.Benzene benz; + parameter Integer Nc = 4; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {hy, nit, ch, benz}; + CyclohexaneTry2.Material Benzene(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-210, -8}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.CentrifugalPump Pump1(C = C, Eff = 0.75, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-180, -10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream Duty1 annotation( + Placement(visible = true, transformation(origin = {-208, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S3A(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-152, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material Hydrogen(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-210, -60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material SRB(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-130, 16}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S5B(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-130, -40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer Mixer(C = C, NI = 4, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-80, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S3B(C = C, Fg = 50, H_p(fixed = false, start = {-10068.1, -30874.3, 473.367}), Nc = Nc, Pg = 2310000, T(fixed = false, start = 310.612), x_pc(fixed = false, start = {{0.65454301, 0.13028786, 0.21320815, 0.0019609832}, {0.00029314764, 0.37909266, 0.6206136, 5.9991806E-07}, {0.98604412, 0.0042212407, 0.0067803513, 0.0029542876}})) annotation( + Placement(visible = true, transformation(origin = {-46, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.ConversionReactor Reactor(BC_r = {4}, C = C, CalcMode = "Isothermal", Coef_cr = {{-3}, {0}, {+1}, {-1}}, Nc = Nc, Nr = 1, Pdel = 103421, X_r = {0.9985}) annotation( + Placement(visible = true, transformation(origin = {-18, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S7(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {10, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream Duty2 annotation( + Placement(visible = true, transformation(origin = {-50, -20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.FlashSeparator Flash1(C = C, Nc = Nc, x_pc(fixed = false)) annotation( + Placement(visible = true, transformation(origin = {50, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S9(C = C, F_p(fixed = false, start = {1.08878, 0, 1.08878}), Fg = 1.08878, Nc = Nc, Pg = 206842, x_pc(fixed = false, start = {{0.870692, 0.112491, 0.0168009, 1.55043E-05}, {0, 0, 0, 0}, {0.870692, 0.112491, 0.0168009, 1.55043E-05}})) annotation( + Placement(visible = true, transformation(origin = {76, 8}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S10(C = C, F_p(fixed = false), Fg = 18.6978, Nc = Nc, Pg = 206842, T(fixed = false, start = 322.039), x_pc(start = {{6.20201E-13, 3.4173E-5, 0.999035, 0.000930975}, {6.20201E-13, 3.4173E-5, 0.999035, 0.000930975}, {0, 0, 0, 0}})) annotation( + Placement(visible = true, transformation(origin = {76, -8}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Splitter Splitter1(C = C, CalcType = "Split_Ratio", Nc = Nc, No = 2) annotation( + Placement(visible = true, transformation(origin = {90, 50}, extent = {{10, -10}, {-10, 10}}, rotation = 0))); + CyclohexaneTry2.Material SROut(C = C, Nc = Nc, x_pc(start = {{0.88368989, 0.096999944, 0.01928136, 2.8805276E-05}, {0.011879885, 0.0023088317, 0.98489395, 0.00091733257}, {0.88369066, 0.097000027, 0.019280511, 2.8804494E-05}})) annotation( + Placement(visible = true, transformation(origin = {110, 80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material SR(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {30, 46}, extent = {{10, -10}, {-10, 10}}, rotation = 0))); + Simulator.UnitOperations.Splitter Splitter2(C = C, CalcType = "Split_Ratio", Nc = Nc, No = 2, Tout_s(start = 322.039)) annotation( + Placement(visible = true, transformation(origin = {30, -50}, extent = {{-10, -10}, {10, 10}}, rotation = -90))); + CyclohexaneTry2.Material S14(C = C, F_p(start = {11.756, 11.756, 0}), Fg = 11.756, Nc = Nc, T(start = 322.039), x_pc(start = {{6.20201E-13, 3.4173E-5, 0.999035, 0.000930975}, {6.20201E-13, 3.4173E-5, 0.999035, 0.000930975}, {0, 0, 0, 0}})) annotation( + Placement(visible = true, transformation(origin = {70, -60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S13(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-10, -72}, extent = {{10, -10}, {-10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve Valve(C = C, Nc = Nc, Tout(start = 315.356)) annotation( + Placement(visible = true, transformation(origin = {102, -60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S14B(C = C, F_p(start = {11.756, 0.034652, 11.7213}), Fg = 11.756, Nc = Nc, P(start = 103421), T(start = 315.356), x_pc(start = {{3.12344e-16, 5.18438e-5, 0.999017, 0.0093112}, {4.4502e-33, 1.07959e-9, 0.97, 0.0361047}, {3.63395e-16, 5.19971e-5, 0.9990716, 0.00923199}}), xm_pc(start = {1, 0.0029476, 0.997052})) annotation( + Placement(visible = true, transformation(origin = {132, -40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.FlashSeparator Flash2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {168, -40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S15(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {202, -32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + CyclohexaneTry2.Material S16(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {202, -48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + connect(Benzene.Out, Pump1.In) annotation( + Line(points = {{-200, -8}, {-190, -8}}, color = {0, 70, 70})); + connect(Duty1.Out, Pump1.En) annotation( + Line(points = {{-198, -30}, {-180, -30}, {-180, -17}}, color = {255, 0, 0})); + connect(Pump1.Out, S3A.In) annotation( + Line(points = {{-170, 0}, {-162, 0}}, color = {0, 70, 70})); + Benzene.F_p[1] = 11.61; +//92.14 lbmol/h is 11.61 mol/s, flowrate of pure benzene + Benzene.x_pc[1, :] = {0, 0, 0, 1}; +//pure benzene + Benzene.T = 310.928; +//100 degF + Benzene.P = 103421; +//15psi + Pump1.Pout = 2310000; +//335psi + Hydrogen.F_p[1] = 35.76; +//hydrogen stream at 283.8 lbmol/h + Hydrogen.x_pc[1, :] = {0.99704, 0.00296, 0, 0}; + Hydrogen.T = 322.039; +//120 degF + Hydrogen.P = 2310000; +//335psi + SRB.F_p[1] = 0.00667834; +//in mol/s + SRB.x_pc[1, :] = {0.88367552, 0.09701428, 0.019281386, 0.000028816624}; + SRB.T = 335.12; +//143.546 degF + SRB.P = 2310000; +// 335 psi + S5B.F_p[1] = 7.20531; +//in mol/s + S5B.x_pc[1, :] = {0.011879037, 0.0023090474, 0.98489423, 0.00091768248}; + S5B.T = 322.15; +//120.201 degF + S5B.P = 2310000; +//335 psi + connect(S3A.Out, Mixer.In[1]) annotation( + Line(points = {{-142, 0}, {-90, 0}}, color = {0, 70, 70})); + connect(Mixer.Out, S3B.In) annotation( + Line(points = {{-70, 0}, {-56, 0}}, color = {0, 70, 70})); + connect(SRB.Out, Mixer.In[2]) annotation( + Line(points = {{-120, 16}, {-90, 16}, {-90, 0}}, color = {0, 70, 70})); + connect(Hydrogen.Out, Mixer.In[3]) annotation( + Line(points = {{-200, -60}, {-154, -60}, {-154, -30}, {-90, -30}, {-90, 0}}, color = {0, 70, 70})); + connect(S5B.Out, Mixer.In[4]) annotation( + Line(points = {{-120, -40}, {-90, -40}, {-90, 0}}, color = {0, 70, 70})); + connect(S3B.Out, Reactor.In) annotation( + Line(points = {{-36, 0}, {-28, 0}, {-28, 0}, {-28, 0}}, color = {0, 70, 70})); + connect(Reactor.Out, S7.In) annotation( + Line(points = {{-8, 0}, {0, 0}, {0, 0}, {0, 0}}, color = {0, 70, 70})); + connect(Duty2.Out, Reactor.energy) annotation( + Line(points = {{-40, -20}, {-18, -20}, {-18, -12}, {-18, -12}}, color = {255, 0, 0})); + connect(Flash1.Out1, S9.In) annotation( + Line(points = {{60, 8}, {66, 8}}, color = {0, 70, 70})); + connect(Flash1.Out2, S10.In) annotation( + Line(points = {{60, -8}, {66, -8}}, color = {0, 70, 70})); + connect(S7.Out, Flash1.In) annotation( + Line(points = {{20, 0}, {40, 0}, {40, 0}, {40, 0}}, color = {0, 70, 70})); + connect(S9.Out, Splitter1.In) annotation( + Line(points = {{86, 8}, {120, 8}, {120, 50}, {100, 50}, {100, 50}}, color = {0, 70, 70})); + connect(SROut.In, Splitter1.Out[2]) annotation( + Line(points = {{100, 80}, {60, 80}, {60, 56}, {80, 56}, {80, 50}, {80, 50}}, color = {0, 70, 70})); + connect(SR.In, Splitter1.Out[1]) annotation( + Line(points = {{40, 46}, {80, 46}, {80, 50}}, color = {0, 70, 70})); + Splitter1.SplRat_s = {0.0082, 0.9918}; + Splitter2.SplRat_s = {0.62, 0.38}; + connect(S10.Out, Splitter2.In) annotation( + Line(points = {{86, -8}, {88, -8}, {88, -40}, {30, -40}, {30, -40}}, color = {0, 70, 70})); + connect(S14.In, Splitter2.Out[1]) annotation( + Line(points = {{60, -60}, {60, -60}, {60, -70}, {36, -70}, {36, -60}, {30, -60}, {30, -60}}, color = {0, 70, 70})); + connect(S13.In, Splitter2.Out[2]) annotation( + Line(points = {{0, -72}, {24, -72}, {24, -60}, {30, -60}}, color = {0, 70, 70})); + connect(S14.Out, Valve.In) annotation( + Line(points = {{80, -60}, {92, -60}, {92, -60}, {92, -60}}, color = {0, 70, 70})); + connect(Valve.Out, S14B.In) annotation( + Line(points = {{112, -60}, {122, -60}, {122, -40}, {122, -40}}, color = {0, 70, 70})); + Valve.Pout = 103421; + connect(S14B.Out, Flash2.In) annotation( + Line(points = {{142, -40}, {158, -40}, {158, -40}, {158, -40}}, color = {0, 70, 70})); + connect(Flash2.Out1, S15.In) annotation( + Line(points = {{178, -32}, {192, -32}, {192, -32}, {192, -32}}, color = {0, 70, 70})); + connect(Flash2.Out2, S16.In) annotation( + Line(points = {{178, -48}, {192, -48}, {192, -48}, {192, -48}}, color = {0, 70, 70})); + connect(S14B.Out, Flash2.In) annotation( + Line(points = {{142, -40}, {158, -40}, {158, -40}, {158, -40}}, color = {0, 70, 70})); + connect(Flash2.Out1, S15.In) annotation( + Line(points = {{178, -32}, {192, -32}, {192, -32}, {192, -32}}, color = {0, 70, 70})); + connect(Flash2.Out2, S16.In) annotation( + Line(points = {{178, -48}, {192, -48}, {192, -48}, {192, -48}}, color = {0, 70, 70})); + end Mainflow; + + model ConversionReactor + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; + end ConversionReactor; + + model FlashSeparator + extends Simulator.UnitOperations.Flash; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end FlashSeparator; + + model AdiabComp + extends Simulator.UnitOperations.AdiabaticCompressor; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end AdiabComp; +end CyclohexaneTry2; diff --git a/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheetAbstract.pdf b/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheetAbstract.pdf new file mode 100644 index 0000000..d095cb5 Binary files /dev/null and b/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/CyclohexaneFlowsheetAbstract.pdf differ diff --git a/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/README.txt b/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/README.txt new file mode 100644 index 0000000..8a1dc33 --- /dev/null +++ b/Production_Of_Cyclohexane_Through_Catalytic_Hydrogenation_Of_Benzene_By_Mr_Kshitij_Sovanee/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Production of Cyclohexane through Catalytic Hydrogenation of Benzene +Proposar Name: Mr Kshitij Sovanee +University: Indian Institute of Technology Bombay + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/Diethyl.mo b/Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/Diethyl.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/README.txt b/Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/abstract_diethylether.pdf b/Production_Of_Diethyl_Ether_From_Ethanol_By_Dehydration_By_Mr_Malapati_Sree_Harsha/abstract_diethylether.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/Dimethylether_Production_Abstract.pdf b/Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/Dimethylether_Production_Abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/Dimethylether_Production_Flowsheet.mo b/Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/Dimethylether_Production_Flowsheet.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/README.txt b/Production_Of_Dimethyl_Ether_By_Ms_Ayushi_Sinha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/README.txt b/Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/abstract.pdf b/Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/ethylchloride.mo b/Production_Of_Ethyl_Chloride_From_Ethylene_Involving_Recycle_Stream_By_Mr_Malapati_Sree_Harsha/ethylchloride.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/Abstract.pdf b/Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/README.txt b/Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/ethyleneOxide.mo b/Production_Of_Ethylene_Oxide_By_Mr_Malapati_Sree_Harsha/ethyleneOxide.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/Production_of_Hydrogen_using_WGRS.pdf b/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/Production_of_Hydrogen_using_WGRS.pdf new file mode 100644 index 0000000..f7ce4e5 Binary files /dev/null and b/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/Production_of_Hydrogen_using_WGRS.pdf differ diff --git a/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/README.txt b/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/README.txt new file mode 100644 index 0000000..a41d94a --- /dev/null +++ b/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Production of Hydrogen using Water Gas Shift Reaction +Proposar Name: Ms Patel Bharvi +University: Sardar Vallabhbhai National Institute of Technology, Surat + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/wgrs.mo b/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/wgrs.mo new file mode 100644 index 0000000..2ff1f3a --- /dev/null +++ b/Production_Of_Hydrogen_Using_Water_Gas_Shift_Reaction_By_Ms_Patel_Bharvi/wgrs.mo @@ -0,0 +1,117 @@ +package wgrs +model MS "Extension of Material Stream with Raoult's Law" + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +annotation( + Documentation(info = "This is a non-executable model is created inside the package Heater to extend the MaterialStream model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the HeaterSimulation model to create the required number of instances of the material stream model.
")); +end MS; + +model ConvReactor "Extension of Conversion Reactor with Conversion Reaction" + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; +annotation( + Documentation(info = "This is a non-executable model is created inside the package CR to extend the ConversionReactor model along with the necessary reaction from Reaction Manager which is ConversionReaction in this case.

It will be instantiated in the ConvReactSimulation model to create the required number of instances of the adiabatic expander model.
")); +end ConvReactor; + +model ConvReactor2 "Extension of Conversion Reactor with Conversion Reaction" + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; +annotation( + Documentation(info = "This is a non-executable model is created inside the package CR to extend the ConversionReactor model along with the necessary reaction from Reaction Manager which is ConversionReaction in this case.

It will be instantiated in the ConvReactSimulation model to create the required number of instances of the adiabatic expander model.
")); +end ConvReactor2; + +model FlashSep "Extension of Flash Separator with Raoult's Law" + extends Simulator.UnitOperations.Flash; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "This is a non-executable model is created inside the package Flash to extend the FlashColumn model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the FlashSimulation model to create the required instance of the flash column model.
")); +end FlashSep; + +model flowsheet1 + import data = Simulator.Files.ChemsepDatabase; + parameter Integer Nc = 7; + parameter data.Methane Im; + parameter data.Oxygen Io; + parameter data.Water Iw; + parameter data.Nitrogen In; + parameter data.Carbonmonoxide Icm; + parameter data.Carbondioxide Icd; + parameter data.Hydrogen Ih; + parameter data.GeneralProperties C[Nc] = {Im, Io, Iw, In, Icm, Icd, Ih}; + wgrs.MS M1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-356, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler C1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-312, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-292, -40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.MS M2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-264, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.MS M3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-152, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler C2(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-100,0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E3 annotation( + Placement(visible = true, transformation(origin = {-80, -40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.MS M4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-52, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.ConvReactor R1(BC_r = {3}, C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{0}, {0}, {-1}, {0}, {-1}, {1}, {1}}, Nc = Nc, Nr = 1, Pdel = 0, Tdef = 698.15, X_r = {0.316389}) annotation( + Placement(visible = true, transformation(origin = {-202, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.ConvReactor2 R2(BC_r = {3}, C = C, Nc = Nc, Nr = 1,CalcMode = "Define_Out_Temperature", Coef_cr = {{0}, {0}, {-1}, {0}, {-1}, {1}, {1}}, Pdel = 0, Tdef = 473.15, X_r = {1.36424E-10}) annotation( + Placement(visible = true, transformation(origin = {0, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); +wgrs.MS M5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {44, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler C3(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {90, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E4 annotation( + Placement(visible = true, transformation(origin = {110, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.MS M6(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {140, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.FlashSep S1(BTdef = true, C = C, Nc = Nc, Tdef = 298.15) annotation( + Placement(visible = true, transformation(origin = {184, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.MS M7(C = C, Nc = Nc, x_pc(fixed = false, start = {{0.0191701, 0.00883654, 0.00782673, 0.337004, 0.469562, 5.8286E-15, 0.157329}, {0.000123826, 1.10726E-05, 0.830742, 5.96678E-05, 0.000254449, 3.66669E-16, 2.72066e-16}, {0.0192007, 0.00885072, 0.00650491, 0.337546, 0.470316, 5.83738E-15, 0.157582}})) annotation( + Placement(visible = true, transformation(origin = {230, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + wgrs.MS M8(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {228, -6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + M1.P = 405300; + M1.T = 617.15; + M1.F_p[1] = 4.709; + M1.x_pc[1, :] = {0.016139308, 0.0074325759, 0.24230197, 0.28349968, 0.076661712, 0.05563814, 0.31832661}; + connect(M1.Out, C1.In) annotation( + Line(points = {{-346, 0}, {-322, 0}}, color = {0, 70, 70})); + C1.Out.T = 589.15; + connect(C1.Out, M2.In) annotation( + Line(points = {{-302, 0}, {-274, 0}}, color = {0, 70, 70})); + connect(C1.En, E1.In) annotation( + Line(points = {{-302, -10}, {-302, -40}}, color = {255, 0, 0})); + connect(M3.Out, C2.In) annotation( + Line(points = {{-142, 0}, {-110, 0}}, color = {0, 70, 70})); + connect(C2.En, E3.In) annotation( + Line(points = {{-90, -10}, {-90, -40}}, color = {255, 0, 0})); + connect(C2.Out, M4.In) annotation( + Line(points = {{-90, 0}, {-62, 0}}, color = {0, 70, 70})); + C2.Out.T = 471.15; + connect(R1.Out, M3.In) annotation( + Line(points = {{-192, 0}, {-162, 0}}, color = {0, 70, 70})); + connect(M2.Out, R1.In) annotation( + Line(points = {{-254, 0}, {-212, 0}}, color = {0, 70, 70})); + connect(M4.Out, R2.In) annotation( + Line(points = {{-42, 0}, {-10, 0}, {-10, 0}, {-10, 0}, {-10, 0}}, color = {0, 70, 70})); + connect(R2.Out, M5.In) annotation( + Line(points = {{10, 0}, {36, 0}, {36, 0}, {34, 0}, {34, 0}}, color = {0, 70, 70})); + connect(M5.Out, C3.In) annotation( + Line(points = {{54, 0}, {80, 0}, {80, 0}, {80, 0}}, color = {0, 70, 70})); + connect(C3.En, E4.In) annotation( + Line(points = {{100, -10}, {100, -38}}, color = {255, 0, 0})); + C3.Out.T = 333.15; + connect(C3.Out, M6.In) annotation( + Line(points = {{100, 0}, {130, 0}}, color = {0, 70, 70})); + connect(M6.Out, S1.In) annotation( + Line(points = {{150, 0}, {174, 0}, {174, 2}, {174, 2}}, color = {0, 70, 70})); + connect(S1.Out1, M7.In) annotation( + Line(points = {{194, 10}, {220, 10}}, color = {0, 70, 70})); + connect(S1.Out2, M8.In) annotation( + Line(points = {{194, -6}, {218, -6}}, color = {0, 70, 70})); + end flowsheet1; + +end wgrs; diff --git a/Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/Methanation_System.pdf b/Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/Methanation_System.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/Methanation_system.mo b/Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/Methanation_system.mo old mode 100755 new mode 100644 diff --git a/Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/README.txt b/Production_Of_Methane_From_Carbon_Monoxide_And_Hydrogen_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/README.txt b/Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/methanolNew.mo b/Production_Of_Methanol_By_Mr_Neel_Pulin_Modi/methanolNew.mo old mode 100755 new mode 100644 diff --git a/Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.mo b/Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.mo new file mode 100644 index 0000000..6876ecc --- /dev/null +++ b/Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.mo @@ -0,0 +1,483 @@ +package N_Octane + model ms + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end ms; + + + model react + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; + end react; + + +model flowsheet + extends Modelica.Icons.Example; + parameter Integer Nc = 5; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Ethylene eth; + parameter data.Isobutane ibut; + parameter data.Nbutane nbut; + parameter data.Nitrogen nitro; + parameter data.Noctane noct; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {eth, ibut, nbut, nitro, noct}; + N_Octane.ms recycle(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-418, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S1(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-322, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Examples.Expander.AdiabExp B1(Nc = Nc, C = C, Eff = 0.75) annotation( + Placement(visible = true, transformation(origin = {-375, 101}, extent = {{-15, -15}, {15, 15}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-416, 42}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S2(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-322, 158}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-216, 128}, extent = {{-16, -16}, {16, 16}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer1(C = C, Nc = Nc, NI = 2, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-265, 129}, extent = {{-13, -13}, {13, 13}}, rotation = 0))); + N_Octane.ms S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-130, 128}, extent = {{-14, -14}, {14, 14}}, rotation = 0))); + Simulator.UnitOperations.Heater heater1(Pdel = 0, Eff = 1, Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-174, 128}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {-196, 64}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {34, 128}, extent = {{-14, -14}, {14, 14}}, rotation = 0))); + N_Octane.react B2(BC_r = {1}, C = C, CalcMode = "Isothermal", Pdel = 48263.2, Coef_cr = {{-2}, {-1}, {0}, {0}, {1}}, Nc = Nc, Nr = 1, X_r = {0.98}) annotation( + Placement(visible = true, transformation(origin = {-60, 128}, extent = {{-18, -18}, {18, 18}}, rotation = 0))); + Simulator.Streams.EnergyStream E3 annotation( + Placement(visible = true, transformation(origin = {-84, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.fls FLASH(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {80, 132}, extent = {{-14, -14}, {14, 14}}, rotation = 0))); + N_Octane.ms Gas(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {128, 150}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms Liquid(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {128, 80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S6(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {270, 24}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S7(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {270, 82}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E4 annotation( + Placement(visible = true, transformation(origin = {268, 104}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E5 annotation( + Placement(visible = true, transformation(origin = {268, -26}, extent = {{10, -10}, {-10, 10}}, rotation = 0))); + N_Octane.DistColumn DC1(C = C, InT_s = {2}, Nc = Nc, Ni = 1, Nt = 3) annotation( + Placement(visible = true, transformation(origin = {214, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S8(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {368, 134}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S9(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {372, 58}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Splitter B3(Nc = Nc, C = C, No = 2, CalcType = "Split_Ratio") annotation( + Placement(visible = true, transformation(origin = {320, 82}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + N_Octane.ms S10(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {490, 124}, extent = {{-10, -10}, {10, 10}}, rotation = -90))); + Simulator.UnitOperations.Heater heater2(Pdel = 0, Eff = 1, Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {422, 134}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E6 annotation( + Placement(visible = true, transformation(origin = {410, 88}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Examples.Compressor.AdiabComp B4(Nc = Nc, C = C, Eff = 0.75) annotation( + Placement(visible = true, transformation(origin = {529, 111}, extent = {{-15, -15}, {15, 15}}, rotation = 0))); + N_Octane.ms S11(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {618, 114}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E7 annotation( + Placement(visible = true, transformation(origin = {566, 48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler B5(Pdel = 0, Eff = 1, Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {658, 114}, extent = {{-14, -14}, {14, 14}}, rotation = 0))); + N_Octane.ms S12(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {716, 116}, extent = {{-12, -12}, {12, 12}}, rotation = 0))); + Simulator.Streams.EnergyStream E8 annotation( + Placement(visible = true, transformation(origin = {681, 55}, extent = {{-13, -13}, {13, 13}}, rotation = 0))); + equation + connect(B5.En, E8.In) annotation( + Line(points = {{672, 100}, {668, 100}, {668, 56}, {668, 56}}, color = {255, 0, 0})); + connect(B5.Out, S12.In) annotation( + Line(points = {{672, 114}, {704, 114}, {704, 116}, {704, 116}}, color = {0, 70, 70})); + connect(S11.Out, B5.In) annotation( + Line(points = {{628, 114}, {644, 114}, {644, 114}, {644, 114}}, color = {0, 70, 70})); + connect(E7.Out, B4.En) annotation( + Line(points = {{576, 48}, {529, 48}, {529, 101}}, color = {255, 0, 0})); + connect(S10.Out, B4.In) annotation( + Line(points = {{490, 114}, {492, 114}, {492, 111}, {514, 111}}, color = {0, 70, 70})); + connect(B4.Out, S11.In) annotation( + Line(points = {{544, 111}, {544, 114}, {608, 114}}, color = {0, 70, 70})); + connect(E1.Out, B1.En) annotation( + Line(points = {{-406, 42}, {-406, 79.5}, {-375, 79.5}, {-375, 91}}, color = {255, 0, 0})); + connect(B1.Out, S1.In) annotation( + Line(points = {{-360, 101}, {-360, 100}, {-332, 100}}, color = {0, 70, 70})); + connect(recycle.Out, B1.In) annotation( + Line(points = {{-408, 100}, {-390, 100}, {-390, 101}}, color = {0, 70, 70})); + connect(heater2.Out, S10.In) annotation( + Line(points = {{432, 134}, {490, 134}}, color = {0, 70, 70})); + connect(E6.Out, heater2.En) annotation( + Line(points = {{420, 88}, {422, 88}, {422, 104}, {410, 104}, {410, 124}, {412, 124}, {412, 124}}, color = {255, 0, 0})); + connect(S8.Out, heater2.In) annotation( + Line(points = {{378, 134}, {410, 134}, {410, 134}, {412, 134}}, color = {0, 70, 70})); + connect(B3.Out[1], S9.In) annotation( + Line(points = {{330, 82}, {342, 82}, {342, 58}, {362, 58}, {362, 58}, {362, 58}}, color = {0, 70, 70}, thickness = 0.5)); + connect(B3.Out[2], S8.In) annotation( + Line(points = {{330, 82}, {338, 82}, {338, 134}, {358, 134}, {358, 134}, {358, 134}}, color = {0, 70, 70}, thickness = 0.5)); + connect(S7.Out, B3.In) annotation( + Line(points = {{280, 82}, {310, 82}, {310, 82}, {310, 82}, {310, 82}}, color = {0, 70, 70})); + connect(DC1.Cduty, E4.In) annotation( + Line(points = {{240, 92}, {242, 92}, {242, 104}, {258, 104}, {258, 104}, {258, 104}}, color = {255, 0, 0})); + connect(E5.Out, DC1.Rduty) annotation( + Line(points = {{258, -26}, {240, -26}, {240, -28}, {240, -28}}, color = {255, 0, 0})); + connect(DC1.Bot, S6.In) annotation( + Line(points = {{240, 2}, {252, 2}, {252, 22}, {260, 22}, {260, 24}, {260, 24}}, color = {0, 70, 70})); + connect(DC1.Dist, S7.In) annotation( + Line(points = {{240, 62}, {250, 62}, {250, 82}, {260, 82}, {260, 82}, {260, 82}}, color = {0, 70, 70})); + connect(Gas.Out, DC1.In_s[1]) annotation( + Line(points = {{138, 150}, {170, 150}, {170, 32}, {190, 32}, {190, 32}}, color = {0, 70, 70})); + connect(FLASH.Out2, Liquid.In) annotation( + Line(points = {{94, 120}, {110, 120}, {110, 80}, {118, 80}, {118, 80}, {118, 80}, {118, 80}}, color = {0, 70, 70})); + connect(FLASH.Out1, Gas.In) annotation( + Line(points = {{94, 144}, {110, 144}, {110, 152}, {118, 152}, {118, 150}, {118, 150}, {118, 150}}, color = {0, 70, 70})); + connect(S5.Out, FLASH.In) annotation( + Line(points = {{48, 128}, {56, 128}, {56, 132}, {66, 132}, {66, 132}, {66, 132}}, color = {0, 70, 70})); + connect(S4.Out, B2.In) annotation( + Line(points = {{-116, 128}, {-78, 128}}, color = {0, 70, 70})); + connect(B2.Out, S5.In) annotation( + Line(points = {{-42, 128}, {20, 128}}, color = {0, 70, 70})); + connect(B2.energy, E3.Out) annotation( + Line(points = {{-60, 105}, {-60, 32}, {-74, 32}}, color = {255, 0, 0})); + connect(E2.Out, heater1.En) annotation( + Line(points = {{-186, 64}, {-180, 64}, {-180, 104}, {-188, 104}, {-188, 114}, {-184, 114}, {-184, 118}, {-184, 118}}, color = {255, 0, 0})); + connect(heater1.Out, S4.In) annotation( + Line(points = {{-164, 128}, {-144, 128}, {-144, 128}, {-144, 128}}, color = {0, 70, 70})); + connect(S3.Out, heater1.In) annotation( + Line(points = {{-200, 128}, {-184, 128}, {-184, 130}, {-184, 130}, {-184, 128}, {-184, 128}, {-184, 128}}, color = {0, 70, 70})); + connect(mixer1.Out, S3.In) annotation( + Line(points = {{-252, 130}, {-232, 130}, {-232, 128}, {-232, 128}}, color = {0, 70, 70})); + connect(S1.Out, mixer1.In[1]) annotation( + Line(points = {{-312, 100}, {-306, 100}, {-306, 124}, {-278, 124}, {-278, 128}, {-278, 128}, {-278, 130}}, color = {0, 70, 70})); + connect(S2.Out, mixer1.In[2]) annotation( + Line(points = {{-312, 158}, {-304, 158}, {-304, 130}, {-278, 130}, {-278, 130}, {-278, 130}}, color = {0, 70, 70})); + recycle.x_pc[1, :] = {0, 0, 0.044, 0, 0.95}; + recycle.P = 165476; + recycle.T = 366.15; + recycle.F_p[1] = 0.892719; + B1.Pdel = 27581; + S2.x_pc[1, :] = {0.6536, 0.3268, 0.0163, 0.0033, 0}; + S2.P = 137896; + S2.T = 366.15; + S2.F_p[1] = 8.5; + S4.T = 366.15; + DC1.condenser.P = 101325; + DC1.reboiler.P = 101325; + DC1.RR = 1.608; + S6.x_pc[1, 5] = 0.7713; + B3.SpecVal_s = {0.9, 0.1}; + S10.T = 366.15; + B4.Pdel = 50361; + S12.T = 366.15; + end flowsheet; + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + model AdiabExp + extends Simulator.UnitOperations.AdiabaticExpander; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end AdiabExp; + + model Condensor + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Condensor; + + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Tray; + + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Reboiler; + + + + model DistColumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end DistColumn; + + model AdiabComp + extends Simulator.UnitOperations.AdiabaticCompressor; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end AdiabComp; + + model fls + extends Simulator.UnitOperations.Flash; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end fls; + + + + + + + + + + + + + + + + + + + +end N_Octane; diff --git a/Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.pdf b/Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.pdf new file mode 100644 index 0000000..e479bd3 Binary files /dev/null and b/Production_Of_N-Octane_From_Ethylene_And_I-Butane_By_Mr_Sandeep_Kumar_Samanta/N_Octane.pdf differ diff --git a/Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/Flowsheet_ProductionOfParaxylene.mo b/Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/Flowsheet_ProductionOfParaxylene.mo old mode 100755 new mode 100644 diff --git a/Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/README.txt b/Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/abstract.pdf b/Production_Of_P-Xylene_By_Mr_Malapati_Sree_Harsha/abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Production_Of_Toluene_By_Dehydration_of_Normal_Heptane.pdf b/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Production_Of_Toluene_By_Dehydration_of_Normal_Heptane.pdf new file mode 100644 index 0000000..43b21e7 Binary files /dev/null and b/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Production_Of_Toluene_By_Dehydration_of_Normal_Heptane.pdf differ diff --git a/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/README.txt b/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/README.txt new file mode 100644 index 0000000..2bc95c6 --- /dev/null +++ b/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Production of Toluene by Dehydrogenation of Normal Heptane +Proposar Name: Mr Aniruddh Mukunth +University: SASTRA Deemed to be University + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Toluene.mo b/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Toluene.mo new file mode 100644 index 0000000..3681ce1 --- /dev/null +++ b/Production_Of_Toluene_By_Dehydrogenation_Of_Normal_Heptane_By_Mr_Aniruddh_Mukunth/Toluene.mo @@ -0,0 +1,80 @@ +package Toluene + model flowsheet + extends Modelica.Icons.Example; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Toluene tol; + parameter data.Nheptane nhep; + parameter data.Hydrogen h; + parameter Integer Nc = 3; + parameter data.GeneralProperties C[Nc] = {tol,nhep,h}; + Toluene.ms S1(C=C,Nc=Nc) annotation( + Placement(visible = true, transformation(origin = {-204, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater heater1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-158, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Toluene.ms S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-120, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-184, 12}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Toluene.conv_react CR1(BC_r = {2}, C = C, Coef_cr = {{1}, {-1}, {4}}, Nc = Nc, Nr = 1, X_r = {0.15}) annotation( + Placement(visible = true, transformation(origin = {-86, 28}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {-100, -4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Toluene.ms S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-54, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-22, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Toluene.ms S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {12, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E3 annotation( + Placement(visible = true, transformation(origin = {0, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Toluene.FlashSep flashSep1(BTdef = true,C = C, Nc = Nc, Tdef = 291.483) annotation( + Placement(visible = true, transformation(origin = {44, 30}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Toluene.ms S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {78, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Toluene.ms S6(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {76, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S1.T = 291.483; + S1.P = 101325; + S1.F_p[1] = 9.97984; + S1.x_pc[1, :] = {0, 1, 0}; + S2.T = 699.817; + cooler1.Tout=293; + connect(S1.Out, heater1.In) annotation( + Line(points = {{-194, 28}, {-168, 28}}, color = {0, 70, 70})); + connect(E1.Out, heater1.En) annotation( + Line(points = {{-174, 12}, {-168, 12}, {-168, 18}}, color = {255, 0, 0})); + connect(heater1.Out, S2.In) annotation( + Line(points = {{-148, 28}, {-130, 28}}, color = {0, 70, 70})); + connect(S2.Out, CR1.In) annotation( + Line(points = {{-110, 28}, {-96, 28}}, color = {0, 70, 70})); + connect(E2.Out, CR1.energy) annotation( + Line(points = {{-90, -4}, {-86, -4}, {-86, 16}}, color = {255, 0, 0})); + connect(CR1.Out, S3.In) annotation( + Line(points = {{-76, 28}, {-64, 28}}, color = {0, 70, 70})); + connect(S3.Out, cooler1.In) annotation( + Line(points = {{-44, 28}, {-38, 28}, {-38, 28}, {-32, 28}}, color = {0, 70, 70})); + connect(cooler1.En, E3.In) annotation( + Line(points = {{-12, 18}, {-10, 18}, {-10, 10}}, color = {255, 0, 0})); + connect(cooler1.Out, S4.In) annotation( + Line(points = {{-12, 28}, {2, 28}}, color = {0, 70, 70})); + connect(flashSep1.Out1, S5.In) annotation( + Line(points = {{54, 38}, {68, 38}}, color = {0, 70, 70})); + connect(flashSep1.Out2, S6.In) annotation( + Line(points = {{54, 22}, {66, 22}}, color = {0, 70, 70})); + connect(S4.Out, flashSep1.In) annotation( + Line(points = {{22, 28}, {34, 28}, {34, 30}}, color = {0, 70, 70})); + end flowsheet; +model ms + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end ms; +model conv_react + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; +end conv_react; +model FlashSep + extends Simulator.UnitOperations.Flash; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end FlashSep; +end Toluene; diff --git a/Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/README.txt b/Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/README.txt old mode 100755 new mode 100644 diff --git a/Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/VinylChloride_Production_Abstract.pdf b/Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/VinylChloride_Production_Abstract.pdf old mode 100755 new mode 100644 diff --git a/Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/VinylChloride_Production_Flowsheet.mo b/Production_Of_Vinyl_Chloride_Monomer_Via_Acetylene-Hcl_Reaction_By_Ms_Ayushi_Sinha/VinylChloride_Production_Flowsheet.mo old mode 100755 new mode 100644 diff --git a/Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/Abstract.pdf b/Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/Abstract.pdf old mode 100755 new mode 100644 diff --git a/Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/MethanolTolueneExtractiveNew.mo b/Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/MethanolTolueneExtractiveNew.mo old mode 100755 new mode 100644 diff --git a/Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/README.txt b/Psd_For_Methanol-Toluene_Separation_Using_Light_Entrainer_Chloroform_By_Mr_Neel_Pulin_Modi/README.txt old mode 100755 new mode 100644 diff --git a/Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/Abstract.pdf b/Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/Abstract.pdf new file mode 100644 index 0000000..f1cc1e0 Binary files /dev/null and b/Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/Abstract.pdf differ diff --git a/Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/flowsheet.mo b/Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/flowsheet.mo new file mode 100644 index 0000000..3c3d109 --- /dev/null +++ b/Regenerative_Rankine_Cycle_By_Mr_Sandeep_Kumar_Samanta/flowsheet.mo @@ -0,0 +1,136 @@ +package T1 + model ms + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end ms; + + model flowsheet + extends Modelica.Icons.Example; + parameter Integer Nc = 1; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Water wat; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {wat}; + T1.ms S1(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-390, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Examples.Expander.AdiabExp B1(Nc = Nc, C = C, Eff = 1) annotation( + Placement(visible = true, transformation(origin = {-333, 121}, extent = {{-15, -15}, {15, 15}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-344, 80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + T1.ms S2(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-290, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + T1.ms S3(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-230, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {-250, 80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler B2(Pdel = 0, Eff = 1, Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-259, 119}, extent = {{-11, -11}, {11, 11}}, rotation = 0))); + T1.ms S4(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-150, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + T1.ms S5(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-150, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Splitter B3(Nc = Nc, C = C, No = 2, CalcType = "Split_Ratio") annotation( + Placement(visible = true, transformation(origin = {-190, 70}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E4 annotation( + Placement(visible = true, transformation(origin = {-108, 80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler B4(Pdel = 7000, Eff = 1, Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-109, 121}, extent = {{-11, -11}, {11, 11}}, rotation = 0))); + T1.ms S6(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-70, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve B5(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {-31, 121}, extent = {{-11, -11}, {11, 11}}, rotation = 0))); + T1.ms S7(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {6, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.CentrifugalPump B6(C = C, Nc = Nc, Eff = 1) annotation( + Placement(visible = true, transformation(origin = {52, 112}, extent = {{-14, -14}, {14, 14}}, rotation = 0))); + Simulator.Streams.EnergyStream E6 annotation( + Placement(visible = true, transformation(origin = {30, 60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + T1.ms S8(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {90, 100}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer B7(Nc = Nc, NI = 2, C = C, outPress = "Inlet_Maximum") annotation( + Placement(visible = true, transformation(origin = {133, 29}, extent = {{-11, -11}, {11, 11}}, rotation = 0))); + T1.ms S9(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {192, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.CentrifugalPump B8(C = C, Nc = Nc, Eff = 1) annotation( + Placement(visible = true, transformation(origin = {236, 32}, extent = {{-14, -14}, {14, 14}}, rotation = 0))); + Simulator.Streams.EnergyStream E8 annotation( + Placement(visible = true, transformation(origin = {210, -20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + T1.ms S10(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {290, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E9 annotation( + Placement(visible = true, transformation(origin = {311, -19}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Simulator.UnitOperations.Heater B9(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {332, 34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + T1.ms S11(Nc = Nc, C = C) annotation( + Placement(visible = true, transformation(origin = {372, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + connect(S1.Out, B1.In) annotation( + Line(points = {{-380, 100}, {-364, 100}, {-364, 121}, {-348, 121}}, color = {0, 70, 70})); + connect(B1.Out, S2.In) annotation( + Line(points = {{-318, 121}, {-309, 121}, {-309, 100}, {-300, 100}}, color = {0, 70, 70})); + connect(E1.Out, B1.En) annotation( + Line(points = {{-334, 80}, {-333, 80}, {-333, 111}}, color = {255, 0, 0})); + S1.x_pc[1, :] = {1}; + S1.P = 9E+06; + S1.T = 1506.04; + S1.F_p[1] = 21.6483; + B1.Pdel = -10; + S3.T = 1493.89; + B3.SpecVal_s = {0.6, 0.4}; + S6.T = 1460.8; + B5.Pdel = 0; + B6.Q = 12279; + B8.Pdel = 7; + S11.T = 1506.04; + connect(S2.Out, B2.In) annotation( + Line(points = {{-280, 100}, {-278, 100}, {-278, 119}, {-270, 119}}, color = {0, 70, 70})); + connect(B2.Out, S3.In) annotation( + Line(points = {{-248, 120}, {-242, 120}, {-242, 100}, {-240, 100}}, color = {0, 70, 70})); + connect(B2.En, E2.In) annotation( + Line(points = {{-248, 108}, {-248, 108}, {-248, 90}, {-266, 90}, {-266, 80}, {-260, 80}, {-260, 80}}, color = {255, 0, 0})); + connect(S3.Out, B3.In) annotation( + Line(points = {{-220, 100}, {-210, 100}, {-210, 70}, {-200, 70}, {-200, 70}}, color = {0, 70, 70})); + connect(B3.Out[1], S4.In) annotation( + Line(points = {{-180, 70}, {-172, 70}, {-172, 100}, {-160, 100}, {-160, 100}, {-160, 100}}, color = {0, 70, 70})); + connect(B3.Out[2], S5.In) annotation( + Line(points = {{-180, 70}, {-172, 70}, {-172, 40}, {-160, 40}, {-160, 40}}, color = {0, 70, 70})); + connect(S4.Out, B4.In) annotation( + Line(points = {{-140, 100}, {-134, 100}, {-134, 122}, {-120, 122}, {-120, 122}}, color = {0, 70, 70})); + connect(B4.Out, S6.In) annotation( + Line(points = {{-98, 122}, {-86, 122}, {-86, 102}, {-80, 102}, {-80, 100}}, color = {0, 70, 70})); + connect(B4.En, E4.In) annotation( + Line(points = {{-98, 110}, {-98, 110}, {-98, 88}, {-118, 88}, {-118, 80}, {-118, 80}}, color = {255, 0, 0})); + connect(S6.Out, B5.In) annotation( + Line(points = {{-60, 100}, {-54, 100}, {-54, 121}, {-42, 121}}, color = {0, 70, 70})); + connect(B5.Out, S7.In) annotation( + Line(points = {{-20, 121}, {-6, 121}, {-6, 98}, {-4, 98}, {-4, 100}}, color = {0, 70, 70})); + connect(S7.Out, B6.In) annotation( + Line(points = {{16, 100}, {22, 100}, {22, 114}, {38, 114}, {38, 114}, {38, 114}}, color = {0, 70, 70})); + connect(B6.Out, S8.In) annotation( + Line(points = {{66, 126}, {72, 126}, {72, 100}, {80, 100}, {80, 100}}, color = {0, 70, 70})); + connect(E6.Out, B6.En) annotation( + Line(points = {{40, 60}, {50, 60}, {50, 102}, {52, 102}, {52, 102}}, color = {255, 0, 0})); + connect(S8.Out, B7.In[1]) annotation( + Line(points = {{100, 100}, {110, 100}, {110, 30}, {122, 30}, {122, 30}}, color = {0, 70, 70})); + connect(S5.Out, B7.In[2]) annotation( + Line(points = {{-140, 40}, {-124, 40}, {-124, 16}, {110, 16}, {110, 30}, {122, 30}, {122, 30}}, color = {0, 70, 70})); + connect(B7.Out, S9.In) annotation( + Line(points = {{144, 30}, {152, 30}, {152, 40}, {184, 40}, {184, 40}, {182, 40}, {182, 40}}, color = {0, 70, 70})); + connect(S9.Out, B8.In) annotation( + Line(points = {{202, 40}, {210, 40}, {210, 36}, {222, 36}, {222, 34}, {222, 34}}, color = {0, 70, 70})); + connect(B8.Out, S10.In) annotation( + Line(points = {{250, 46}, {262, 46}, {262, 40}, {280, 40}, {280, 40}}, color = {0, 70, 70})); + connect(E8.Out, B8.En) annotation( + Line(points = {{220, -20}, {236, -20}, {236, 22}, {236, 22}, {236, 22}}, color = {255, 0, 0})); + connect(E9.Out, B9.En) annotation( + Line(points = {{320, -18}, {328, -18}, {328, 0}, {322, 0}, {322, 24}, {322, 24}}, color = {255, 0, 0})); + connect(S10.Out, B9.In) annotation( + Line(points = {{300, 40}, {308, 40}, {308, 34}, {322, 34}, {322, 34}, {322, 34}}, color = {0, 70, 70})); + connect(B9.Out, S11.In) annotation( + Line(points = {{342, 34}, {352, 34}, {352, 40}, {362, 40}, {362, 40}, {362, 40}}, color = {0, 70, 70})); + end flowsheet; + + model AdiabExp + extends Simulator.UnitOperations.AdiabaticExpander; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end AdiabExp; +end T1; diff --git a/Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/Iso1.mo b/Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/Iso1.mo old mode 100755 new mode 100644 diff --git a/Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/README.txt b/Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/README.txt old mode 100755 new mode 100644 diff --git a/Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/Tanay_Removal_of_Isopentane.pdf b/Removal_Of_Isopentane_In_Gasoline_Tower_By_Mr_Tanay_Kedia/Tanay_Removal_of_Isopentane.pdf old mode 100755 new mode 100644 diff --git a/Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/Abstract_OM.pdf b/Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/Abstract_OM.pdf old mode 100755 new mode 100644 diff --git a/Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/Air_benzene_separation.mo b/Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/Air_benzene_separation.mo old mode 100755 new mode 100644 diff --git a/Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/README.txt b/Separation_Of_Benzene_From_Air_Using_Compression_By_Ms_Aditi_Jain/README.txt old mode 100755 new mode 100644 diff --git a/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/Abstract_Separation_of_Pyridine_and_Water_using_PSD.pdf b/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/Abstract_Separation_of_Pyridine_and_Water_using_PSD.pdf new file mode 100644 index 0000000..4ca171f Binary files /dev/null and b/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/Abstract_Separation_of_Pyridine_and_Water_using_PSD.pdf differ diff --git a/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/PSD.mo b/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/PSD.mo new file mode 100644 index 0000000..65e2bc9 --- /dev/null +++ b/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/PSD.mo @@ -0,0 +1,86 @@ +package PSD + model MSTR + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end MSTR; + + package rigDist + model Condensor + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Condensor; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.NRTL; + end Reboiler; + + model DistColumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end DistColumn; + end rigDist; + + model Flowsheet + import data = Simulator.Files.ChemsepDatabase; + parameter data.Water wat; + parameter data.Pyridine pyr; + parameter Integer Nc = 2; + parameter data.GeneralProperties C[Nc] = {wat, pyr}; + PSD.MSTR S01(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-158, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S02(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-158, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.rigDist.DistColumn DC01(C = C, Ctype = "Total", InT_s = {2, 10}, Nc = Nc, Ni = 2, Nt = 20) annotation( + Placement(visible = true, transformation(origin = {-90, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S03(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-42, 48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S04(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-52, -22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.rigDist.DistColumn DC02(C = C, Ctype = "Total", InT_s = {10}, Nc = Nc, Ni = 1, Nt = 20) annotation( + Placement(visible = true, transformation(origin = { 20, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S06(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {78, -22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S05(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {76, 48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S01.P = 500000; + S01.T = 298.15; + S01.x_pc[1, :] = {0.43, 0.57}; + S01.F_p[1] = 0.78864; + S02.P = 101325; + S02.T = 367.6231; + S02.x_pc[1,:] = {0.7733235, 0.2266765}; + S02.F_p[1] = 0.38557; + DC01.condenser.P = 500000; + DC01.reboiler.P = 500000; + DC01.RR = 1.3; + S04.x_pc[1, 2] = 0.98; + DC02.condenser.P = 101325; + DC02.reboiler.P = 101325; + DC02.RR = 1.3; + S06.x_pc[1, 1] = 0.97; + connect(S02.Out, DC01.In_s[1]) annotation( + Line(points = {{-148, 40}, {-136, 40}, {-136, 18}, {-115, 18}}, color = {0, 70, 70})); + connect(S01.Out, DC01.In_s[2]) annotation( + Line(points = {{-148, 0}, {-136, 0}, {-136, 18}, {-115, 18}}, color = {0, 70, 70})); + connect(DC01.Dist, S03.In) annotation( + Line(points = {{-65, 48}, {-52, 48}}, color = {0, 70, 70})); + connect(DC01.Bot, S04.In) annotation( + Line(points = {{-65, -12}, {-62, -12}, {-62, -22}}, color = {0, 70, 70})); + connect(S03.Out, DC02.In_s[1]) annotation( + Line(points = {{-32, 48}, {-13.5, 48}, {-13.5, 18}, {-5, 18}}, color = {0, 70, 70})); + connect(DC02.Bot, S06.In) annotation( + Line(points = {{45, -12}, {46.5, -12}, {46.5, -22}, {68, -22}}, color = {0, 70, 70})); + connect(DC02.Dist, S05.In) annotation( + Line(points = {{45, 48}, {66, 48}}, color = {0, 70, 70})); + annotation( + Diagram);end Flowsheet; +end PSD; diff --git a/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/README.txt b/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/README.txt new file mode 100644 index 0000000..2192911 --- /dev/null +++ b/Separation_Of_Pyridine_And_Water_Using_Pressure_Swing_Distillation_By_Mr_Ali_Asger/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Separation of Pyridine and Water using Pressure Swing Distillation +Proposar Name: Mr Ali Asger +University: Institute of Chemical Technology, Mumbai Off-Campus Marathwada, Jalna + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/PSD1.mo b/Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/PSD1.mo old mode 100755 new mode 100644 diff --git a/Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/PSD_abstract.pdf b/Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/PSD_abstract.pdf old mode 100755 new mode 100644 diff --git a/Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/README.txt b/Simulation_Of_Pressure_Swing_Distillation_For_Separation_Of_Ethyl_Acetate-Ethanol-Water_By_Mr_Sarthak_Vaidya/README.txt old mode 100755 new mode 100644 diff --git a/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/Abstract.pdf b/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/Abstract.pdf new file mode 100644 index 0000000..1fb8768 Binary files /dev/null and b/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/Abstract.pdf differ diff --git a/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/README.txt b/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/README.txt new file mode 100644 index 0000000..9a0af50 --- /dev/null +++ b/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Syngas Production from Regasified Liquefied Natural Gas +Proposar Name: Mr Aniruddh Mukunth +University: SASTRA Deemed to be University + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/syngas.mo b/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/syngas.mo new file mode 100644 index 0000000..b3a0f00 --- /dev/null +++ b/Syngas_Production_From_Regasified_Liquefied_Natural_Gas_By_Mr_Aniruddh_Mukunth/syngas.mo @@ -0,0 +1,205 @@ +package syngas +model flowsheet + extends Modelica.Icons.Example; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Hydrogen h; + parameter data.Water water; + parameter data.Carbondioxide co2; + parameter data.Carbonmonoxide co; + parameter data.Methane meth; + parameter data.Oxygen oxy; + parameter data.Nitrogen nitro; + parameter Integer Nc = 7; + parameter data.GeneralProperties C[Nc] = {h,water,co2,co,meth,oxy,nitro}; + syngas.ms S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-444, 52}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-444, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer1(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-410, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-378, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater heater1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-350, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-318, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E01 annotation( + Placement(visible = true, transformation(origin = {-378, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {-298, 10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.conv_react conv_react1(BC_r = {5, 5, 4},C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{3, 4, 1}, {-1, -2, -1}, {0, 1, 1}, {1, 0, -1}, {-1, -1, 0}, {0, 0, 0}, {0, 0, 0}}, Nc = Nc, Nr = 3, Pdel = 0, Tdef = 1050.15, X_r = {0.4, 0.3, 1}) annotation( + Placement(visible = true, transformation(origin = {-290, 44}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + syngas.ms S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-258, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S6(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-258, 64}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer2(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Minimum") annotation( + Placement(visible = true, transformation(origin = {-224, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S7(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-190, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E3 annotation( + Placement(visible = true, transformation(origin = {-170, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.conv_react conv_react2(BC_r = {5, 5},C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{0, 0}, {2, 2}, {1, 0}, {0, 1}, {-1, -1}, {-2, -1.5}, {0, 0}}, Nc = Nc, Nr = 2, Pdel = 0, Tdef = 1235.15, X_r = {0.941392, 0.0584}) annotation( + Placement(visible = true, transformation(origin = {-158, 54}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + syngas.ms S8(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-126, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler1(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {-98, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S9(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-72, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E4 annotation( + Placement(visible = true, transformation(origin = {-74, 36}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.EquilibriumReactor ER1(Basis = "PartialPressure", C = C, Coef_cr = {{1}, {-1}, {1}, {-1}, {0}, {0}, {0}}, Kg = {8.3}, Mode = "Define_Out_Temperature", Nc = Nc, Nr = 1, Pdel = 0, Phase = "Vapour", Rmode = "ConstantK", Tdef = 707.15) annotation( + Placement(visible = true, transformation(origin = {-40, 54}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Simulator.Streams.EnergyStream E5 annotation( + Placement(visible = true, transformation(origin = {-50, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S10(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-8, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler2(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {28, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S11(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {60, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E6 annotation( + Placement(visible = true, transformation(origin = {50, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.EquilibriumReactor ER2(Basis = "PartialPressure", C = C, Coef_cr = {{1}, {-1}, {1}, {-1}, {0}, {0}, {0}}, Kg = {99.2}, Mode = "Define_Out_Temperature", Nc = Nc, Nr = 1, Pdel = 0, Phase = "Vapour", Rmode = "ConstantK", Tdef = 501.15) annotation( + Placement(visible = true, transformation(origin = {92, 54}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Simulator.Streams.EnergyStream E7 annotation( + Placement(visible = true, transformation(origin = {80, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S12(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {124, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S13(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {188, 54}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E8 annotation( + Placement(visible = true, transformation(origin = {132, 42}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater heater2(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {160, 56}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.CompoundSeparator CS1(C = C, Nc = Nc, SepFact_c = {"Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent", "Inlet_Molar_Flow_Percent"}, SepStrm = 1) annotation( + Placement(visible = true, transformation(origin = {218, 54}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Simulator.Streams.EnergyStream E9 annotation( + Placement(visible = true, transformation(origin = {226, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S14(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {256, 62}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S15(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {256, 46}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater heater3(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {286, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.ms S16(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {322, 44}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E10 annotation( + Placement(visible = true, transformation(origin = {262, 16}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + syngas.conv_react conv_react3(BC_r = {4, 3}, C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{-3, -4}, {1, 2}, {0, -1}, {-1, 0}, {1, 1}, {0, 0}, {0, 0}}, Nc = Nc, Nr = 2, Tdef = 604.15, X_r = {1, 1}) annotation( + Placement(visible = true, transformation(origin = {352, 44}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + syngas.ms S17(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {384, 42}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E11 annotation( + Placement(visible = true, transformation(origin = {344, 8}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + +equation + S1.P = 3.04E6; + S1.T = 653.15; + S1.F_p[1] = 388.883; + S1.x_pc[1, :] = {0, 1, 0, 0, 0, 0, 0}; + S2.P = 3.73E6; + S2.T = 613.15; + S2.F_p[1] = 138.912; + S2.x_pc[1, :] = {0, 0, 0.00080016003, 0, 0.98519704, 0, 0.014002801}; + S4.T = 753.15; + S6.P = 3.11E6; + S6.T = 1038.15; + S6.F_p[1] = 507.196; + S6.x_pc[1, :] = {0, 0, 0, 0, 0, 0.21, 0.79}; + S9.T = 639.15; + S11.T = 478.15; + S13.T = 523.15; + CS1.SepVal_c = {0, 99, 100, 0, 0, 0,0}; + S16.T=578.15; + connect(S1.Out, mixer1.In[1]) annotation( + Line(points = {{-434, 52}, {-420, 52}, {-420, 44}}, color = {0, 70, 70})); + connect(S2.Out, mixer1.In[2]) annotation( + Line(points = {{-434, 32}, {-420, 32}, {-420, 44}}, color = {0, 70, 70})); + connect(mixer1.Out, S3.In) annotation( + Line(points = {{-400, 44}, {-388, 44}}, color = {0, 70, 70})); + connect(S3.Out, heater1.In) annotation( + Line(points = {{-368, 44}, {-360, 44}}, color = {0, 70, 70})); + connect(E01.Out, heater1.En) annotation( + Line(points = {{-368, 26}, {-364, 26}, {-364, 34}, {-360, 34}}, color = {255, 0, 0})); + connect(heater1.Out, S4.In) annotation( + Line(points = {{-340, 43.8}, {-328, 43.8}}, color = {0, 70, 70})); + connect(S4.Out, conv_react1.In) annotation( + Line(points = {{-308, 44}, {-300, 44}}, color = {0, 70, 70})); + connect(E2.Out, conv_react1.energy) annotation( + Line(points = {{-288, 10}, {-290, 10}, {-290, 32}}, color = {255, 0, 0})); + connect(conv_react1.Out, S5.In) annotation( + Line(points = {{-280, 44}, {-268, 44}}, color = {0, 70, 70})); + connect(S6.Out, mixer2.In[1]) annotation( + Line(points = {{-248, 64}, {-234, 64}, {-234, 54}}, color = {0, 70, 70})); + connect(S5.Out, mixer2.In[2]) annotation( + Line(points = {{-248, 44}, {-234, 44}, {-234, 54}}, color = {0, 70, 70})); + connect(mixer2.Out, S7.In) annotation( + Line(points = {{-214, 54}, {-200, 54}}, color = {0, 70, 70})); + connect(S7.Out, conv_react2.In) annotation( + Line(points = {{-180, 54}, {-168, 54}}, color = {0, 70, 70})); + connect(E3.Out, conv_react2.energy) annotation( + Line(points = {{-160, 22}, {-158, 22}, {-158, 42}}, color = {255, 0, 0})); + connect(conv_react2.Out, S8.In) annotation( + Line(points = {{-148, 54}, {-136, 54}}, color = {0, 70, 70})); + connect(S8.Out, cooler1.In) annotation( + Line(points = {{-116, 54}, {-108, 54}}, color = {0, 70, 70})); + connect(cooler1.En, E4.In) annotation( + Line(points = {{-88, 44}, {-84, 44}, {-84, 36}}, color = {255, 0, 0})); + connect(cooler1.Out, S9.In) annotation( + Line(points = {{-88, 54}, {-82, 54}}, color = {0, 70, 70})); + connect(S9.Out, ER1.In) annotation( + Line(points = {{-62, 54}, {-50, 54}}, color = {0, 70, 70})); + connect(E5.Out, ER1.enConn) annotation( + Line(points = {{-40, 22}, {-40, 42}}, color = {255, 0, 0})); + connect(ER1.Out, S10.In) annotation( + Line(points = {{-30, 54}, {-18, 54}}, color = {0, 70, 70})); + connect(S10.Out, cooler2.In) annotation( + Line(points = {{2, 54}, {18, 54}}, color = {0, 70, 70})); + connect(cooler2.En, E6.In) annotation( + Line(points = {{38, 44}, {40, 44}, {40, 32}}, color = {255, 0, 0})); + connect(cooler2.Out, S11.In) annotation( + Line(points = {{38, 54}, {50, 54}}, color = {0, 70, 70})); + connect(S11.Out, ER2.In) annotation( + Line(points = {{70, 54}, {82, 54}}, color = {0, 70, 70})); + connect(E7.Out, ER2.enConn) annotation( + Line(points = {{90, 20}, {92, 20}, {92, 42}}, color = {255, 0, 0})); + connect(ER2.Out, S12.In) annotation( + Line(points = {{102, 54}, {114, 54}}, color = {0, 70, 70})); + connect(S12.Out, heater2.In) annotation( + Line(points = {{134, 54}, {150, 54}, {150, 56}}, color = {0, 70, 70})); + connect(E8.Out, heater2.En) annotation( + Line(points = {{142, 42}, {150, 42}, {150, 46}}, color = {255, 0, 0})); + connect(heater2.Out, S13.In) annotation( + Line(points = {{170, 55.8}, {174, 55.8}, {174, 53.8}, {178, 53.8}}, color = {0, 70, 70})); + connect(S13.Out, CS1.In) annotation( + Line(points = {{198, 54}, {208, 54}}, color = {0, 70, 70})); + connect(CS1.En, E9.In) annotation( + Line(points = {{218, 41}, {218, 18}, {216, 18}}, color = {255, 0, 0})); + connect(CS1.Out1, S14.In) annotation( + Line(points = {{228, 62}, {246, 62}}, color = {0, 70, 70})); + connect(CS1.Out2, S15.In) annotation( + Line(points = {{228, 46}, {246, 46}}, color = {0, 70, 70})); + connect(S15.Out, heater3.In) annotation( + Line(points = {{266, 46}, {276, 46}, {276, 44}}, color = {0, 70, 70})); + connect(E10.Out, heater3.En) annotation( + Line(points = {{272, 16}, {274, 16}, {274, 34}, {276, 34}}, color = {255, 0, 0})); + connect(heater3.Out, S16.In) annotation( + Line(points = {{296, 43.8}, {312, 43.8}}, color = {0, 70, 70})); + connect(E11.Out, conv_react3.energy) annotation( + Line(points = {{354, 8}, {346, 8}, {346, 12}, {352, 12}, {352, 32}}, color = {255, 0, 0})); + connect(S16.Out, conv_react3.In) annotation( + Line(points = {{332, 44}, {342, 44}}, color = {0, 70, 70})); + connect(conv_react3.Out, S17.In) annotation( + Line(points = {{362, 44}, {374, 44}, {374, 42}}, color = {0, 70, 70})); + end flowsheet; +model ms + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end ms; +model conv_react + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; +end conv_react; +end syngas; diff --git a/Synthesis_Of_Methanol_Using_Open_Modelica_By_Mr_Parimal_Patel/MethanolSynthesis.pdf b/Synthesis_Of_Methanol_Using_Open_Modelica_By_Mr_Parimal_Patel/MethanolSynthesis.pdf deleted file mode 100755 index 6f37243..0000000 Binary files a/Synthesis_Of_Methanol_Using_Open_Modelica_By_Mr_Parimal_Patel/MethanolSynthesis.pdf and /dev/null differ diff --git a/Synthesis_Of_Methanol_Using_Open_Modelica_By_Mr_Parimal_Patel/Methanol_Production.mo b/Synthesis_Of_Methanol_Using_Open_Modelica_By_Mr_Parimal_Patel/Methanol_Production.mo deleted file mode 100755 index 320d382..0000000 --- a/Synthesis_Of_Methanol_Using_Open_Modelica_By_Mr_Parimal_Patel/Methanol_Production.mo +++ /dev/null @@ -1,60 +0,0 @@ -package Methanol_Production - model InletSTRM - // //instantiation of chemsep database - import data = Simulator.Files.Chemsep_Database; - //instantiation of Methanol - parameter data.Methanol metl; - //instantiation of Methane - parameter data.Methane met; - //instantiation of water - parameter data.Water wat; - //instantiation of Carbonmonoxide - parameter data.Carbonmonoxide cmd; - //instantiation of Carbondioxide - parameter data.Carbondioxide cdd; - //instantiation of Hydrogen - parameter data.Hydrogen hgn; - extends Simulator.Streams.Material_Stream(NOC = 6, comp = {metl, met, wat, cmd, cdd, hgn}, totMolFlo(each start = 1), compMolFrac(each start = 0.33), T(start = sum(comp.Tb) / NOC)); - //material stream extended in which parameter NOC and comp are given values and other variables are given start values - extends Simulator.Files.Thermodynamic_Packages.Raoults_Law; - //thermodynamic package Raoults law is extended - end InletSTRM; - - model Conversion_Reactor - extends Simulator.Unit_Operations.Conversion_Reactor; - extends Simulator.Files.Thermodynamic_Packages.Raoults_Law; - - end Conversion_Reactor; - - model Cooler - extends Simulator.Unit_Operations.Cooler; - extends Simulator.Files.Thermodynamic_Packages.Raoults_Law; - - end Cooler; - - model Gas_Liquid_separator - extends Simulator.Unit_Operations.Flash; - extends Simulator.Files.Thermodynamic_Packages.Raoults_Law; - - end Gas_Liquid_separator; - - - - model Compound_separator - extends Simulator.Unit_Operations.Compound_Separator; - extends Simulator.Files.Thermodynamic_Packages.Raoults_Law; - end Compound_separator; - - model Flowsheet - Methanol_Production.InletSTRM inletSTRM1 annotation( - Placement(visible = true, transformation(origin = {-138, 14}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - Conversion_Reactor conversion_Reactor annotation( - Placement(visible = true, transformation(origin = {-86, 14}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); - end Flowsheet; - - - - - - -end Methanol_Production; diff --git a/Synthesis_Of_Methyl_Iodide_From_Hydrogen_Iodide_By_Mr_V.p_Sudharsanarajan/Abstract_Production_of_Methyliodide_from_Hydrogeniodide.pdf b/Synthesis_Of_Methyl_Iodide_From_Hydrogen_Iodide_By_Mr_V.p_Sudharsanarajan/Abstract_Production_of_Methyliodide_from_Hydrogeniodide.pdf new file mode 100644 index 0000000..5ae6b01 Binary files /dev/null and b/Synthesis_Of_Methyl_Iodide_From_Hydrogen_Iodide_By_Mr_V.p_Sudharsanarajan/Abstract_Production_of_Methyliodide_from_Hydrogeniodide.pdf differ diff --git a/Synthesis_Of_Methyl_Iodide_From_Hydrogen_Iodide_By_Mr_V.p_Sudharsanarajan/Flowsheet_Methyliodide.mo b/Synthesis_Of_Methyl_Iodide_From_Hydrogen_Iodide_By_Mr_V.p_Sudharsanarajan/Flowsheet_Methyliodide.mo new file mode 100644 index 0000000..ae6854c --- /dev/null +++ b/Synthesis_Of_Methyl_Iodide_From_Hydrogen_Iodide_By_Mr_V.p_Sudharsanarajan/Flowsheet_Methyliodide.mo @@ -0,0 +1,94 @@ +package Methyliodide_ +model MaterialStream + extends Simulator.Streams.MaterialStream; + end MaterialStream; + + model EnergyStream + extends Simulator.Streams.EnergyStream; + end EnergyStream; + + model ConversionReactor + extends Simulator.UnitOperations.ConversionReactor; + end ConversionReactor; + + model CompoundSeparator + extends Simulator.UnitOperations.CompoundSeparator; + end CompoundSeparator; + +model Mixer + extends Simulator.UnitOperations.Mixer; + end Mixer; + + model Cooler + extends Simulator.UnitOperations.Cooler; + end Cooler; + + + + model Flowsheet + + Methyliodide_.MaterialStream S01(C = C, Fg = 60, Nc = Nc, P(start = 293), Pg = 101325, T(start = 293)) annotation( + Placement(visible = true, transformation(origin = {-256, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.MaterialStream S02(C = C, Nc = Nc) annotation( + + Placement(visible = true, transformation(origin = {-256, -36}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.Mixer mixer annotation( + Placement(visible = true, transformation(origin = {-200, -14}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.ConversionReactor conversionReactor annotation( + Placement(visible = true, transformation(origin = {-152, -12}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Methyliodide_.EnergyStream E01 annotation( + Placement(visible = true, transformation(origin = {-196, -62}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.MaterialStream S03 annotation( + Placement(visible = true, transformation(origin = {-118, 34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.MaterialStream S04 annotation( + Placement(visible = true, transformation(origin = {-114, -52}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.CompoundSeparator compoundSeparator(C = C, Nc = Nc, SepFact_c = Molar_Flow) annotation( + Placement(visible = true, transformation(origin = {-40, 32}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Methyliodide_.MaterialStream S05 annotation( + Placement(visible = true, transformation(origin = {16, 60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.MaterialStream S06 annotation( + Placement(visible = true, transformation(origin = {16, -6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.Mixer ProductMixer annotation( + Placement(visible = true, transformation(origin = {78, -46}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.MaterialStream Product annotation( + Placement(visible = true, transformation(origin = {136, -46}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.Cooler cooler annotation( + Placement(visible = true, transformation(origin = {-80, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Methyliodide_.Cooler cooler1 annotation( + Placement(visible = true, transformation(origin = {-70, -58}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + +equation + connect(S01.Out, mixer.In) annotation( + Line(points = {{-246, 6}, {-210, 6}, {-210, -14}}, color = {0, 70, 70})); + connect(S02.Out, mixer.In) annotation( + Line(points = {{-246, -36}, {-210, -36}, {-210, -14}}, color = {0, 70, 70})); + connect(E01.Out, conversionReactor.energy) annotation( + Line(points = {{-186, -62}, {-186, -46.5}, {-152, -46.5}, {-152, -25}}, color = {255, 0, 0})); + connect(compoundSeparator.Out1, S05.In) annotation( + Line(points = {{-30, 40}, {6, 40}, {6, 60}}, color = {0, 70, 70})); + connect(compoundSeparator.Out2, S06.In) annotation( + Line(points = {{-30, 24}, {6, 24}, {6, -6}}, color = {0, 70, 70})); + connect(mixer.Out, conversionReactor.In) annotation( + Line(points = {{-190, -14}, {-162, -14}, {-162, -12}}, color = {0, 70, 70})); + connect(conversionReactor.Out, S03.In) annotation( + Line(points = {{-142, -12}, {-128, -12}, {-128, 34}}, color = {0, 70, 70})); + connect(conversionReactor.Out, S04.In) annotation( + Line(points = {{-142, -12}, {-124, -12}, {-124, -52}}, color = {0, 70, 70})); + connect(S04.Out, cooler1.In) annotation( + Line(points = {{-104, -52}, {-98, -52}, {-98, -58}, {-80, -58}}, color = {0, 70, 70})); + connect(cooler1.Out, ProductMixer.In) annotation( + Line(points = {{-60, -58}, {68, -58}, {68, -46}}, color = {0, 70, 70})); + connect(S03.Out, cooler.In) annotation( + Line(points = {{-108, 34}, {-90, 34}, {-90, 28}}, color = {0, 70, 70})); + connect(cooler.Out, compoundSeparator.In) annotation( + Line(points = {{-70, 28}, {-50, 28}, {-50, 32}}, color = {0, 70, 70})); + connect(S06.Out, ProductMixer.In) annotation( + Line(points = {{26, -6}, {68, -6}, {68, -46}}, color = {0, 70, 70})); + connect(ProductMixer.Out, Product.In) annotation( + Line(points = {{88, -46}, {126, -46}}, color = {0, 70, 70})); + +end Flowsheet; + + + +end Methyliodide_; diff --git a/Tetrahydrofuran-Water_Pressure_Swing_Azeotropic_Distillation_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/PS_THF_WATER.mo b/Tetrahydrofuran-Water_Pressure_Swing_Azeotropic_Distillation_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/PS_THF_WATER.mo old mode 100755 new mode 100644 diff --git a/Tetrahydrofuran-Water_Pressure_Swing_Azeotropic_Distillation_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/PS_THF_WATER.pdf b/Tetrahydrofuran-Water_Pressure_Swing_Azeotropic_Distillation_By_Mr_Aradhyula_Venkata_Sri_Surya_Praneeth/PS_THF_WATER.pdf old mode 100755 new mode 100644 diff --git a/Using_Catalytic_Reactor_We_Produce_Formaldehyde_By_Mr_Rajan_Sonaimuthu_Ra/Abstract_Production_of_Formaldehyde.pdf b/Using_Catalytic_Reactor_We_Produce_Formaldehyde_By_Mr_Rajan_Sonaimuthu_Ra/Abstract_Production_of_Formaldehyde.pdf new file mode 100644 index 0000000..6e8c13f Binary files /dev/null and b/Using_Catalytic_Reactor_We_Produce_Formaldehyde_By_Mr_Rajan_Sonaimuthu_Ra/Abstract_Production_of_Formaldehyde.pdf differ diff --git a/Using_Catalytic_Reactor_We_Produce_Formaldehyde_By_Mr_Rajan_Sonaimuthu_Ra/flowsheet__Using_catalytic_reactor_we_produce_formaldehyde.mo b/Using_Catalytic_Reactor_We_Produce_Formaldehyde_By_Mr_Rajan_Sonaimuthu_Ra/flowsheet__Using_catalytic_reactor_we_produce_formaldehyde.mo new file mode 100644 index 0000000..20e4189 --- /dev/null +++ b/Using_Catalytic_Reactor_We_Produce_Formaldehyde_By_Mr_Rajan_Sonaimuthu_Ra/flowsheet__Using_catalytic_reactor_we_produce_formaldehyde.mo @@ -0,0 +1,98 @@ +package Formaldehyde_987 + +model materialstream +extends Simulator.Streams.MaterialStream; +extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end materialstream; + +model energystream +extends Simulator.Streams.EnergyStream; +extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +end energystream; + +model catalyticreactor +extends Simulator.UnitOperations.ConversionReactor; +end catalyticreactor; + +model separator +extends Simulator.UnitOperations.CompoundSeparator; +end separator; + +model streammixer +extends Simulator.UnitOperations.Mixer; +end streammixer; + +model recycleblock +extends Simulator.UnitOperations.RecycleBlock; +end recycleblock; + +model methanol + Formaldehyde.materialstream FreshMethanol annotation( + Placement(visible = true, transformation(origin = {-224, 42}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Formaldehyde.materialstream materialstream annotation( + Placement(visible = true, transformation(origin = {-260, -80}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + streammixer mixer(C = C, Fg = 60, NI = 6, Nc = Nc, Pg = 101325, outPress = Inlet_Minimum) annotation( + Placement(visible = true, transformation(origin = {-168, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Formaldehyde.materialstream materialstream1 annotation( + Placement(visible = true, transformation(origin = {-120, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Formaldehyde.energystream energystream annotation( + Placement(visible = true, transformation(origin = {-104, -48}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Formaldehyde.catalyticreactor catalyticreactor annotation( + Placement(visible = true, transformation(origin = {-76, -6}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Formaldehyde.materialstream materialstream2 annotation( + Placement(visible = true, transformation(origin = {-10, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Formaldehyde.materialstream materialstream3 annotation( + Placement(visible = true, transformation(origin = {2, -26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + streammixer streammixer annotation( + Placement(visible = true, transformation(origin = {50, -4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Formaldehyde.materialstream materialstream4 annotation( + Placement(visible = true, transformation(origin = {100, -24}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + catalyticreactor Separator annotation( + Placement(visible = true, transformation(origin = {156, -6}, extent = {{-10, -20}, {10, 20}}, rotation = 0))); + Formaldehyde.energystream energystream1 annotation( + Placement(visible = true, transformation(origin = {130, -62}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + materialstream materialstream5 annotation( + Placement(visible = true, transformation(origin = {220, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + materialstream materialstream6 annotation( + Placement(visible = true, transformation(origin = {216, -34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + recycleblock recycleblock annotation( + Placement(visible = true, transformation(origin = {270, -58}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + +equation + connect(FreshMethanol.Out, mixer.In) annotation( + Line(points = {{-214, 42}, {-178, 42}, {-178, 2}}, color = {0, 70, 70})); + connect(materialstream.Out, mixer.In) annotation( + Line(points = {{-250, -80}, {-178, -80}, {-178, 2}}, color = {0, 70, 70})); + connect(mixer.Out, materialstream1.In) annotation( + Line(points = {{-158, 2}, {-130, 2}, {-130, 28}}, color = {0, 70, 70})); + connect(materialstream1.Out, catalyticreactor.In) annotation( + Line(points = {{-110, 28}, {-86, 28}, {-86, -6}}, color = {0, 70, 70})); + connect(energystream.Out, catalyticreactor.energy) annotation( + Line(points = {{-94, -48}, {-76, -48}, {-76, -19}}, color = {255, 0, 0})); + connect(catalyticreactor.Out, materialstream2.In) annotation( + Line(points = {{-66, -6}, {-20, -6}, {-20, 18}}, color = {0, 70, 70})); + connect(catalyticreactor.Out, materialstream3.In) annotation( + Line(points = {{-66, -6}, {-8, -6}, {-8, -26}}, color = {0, 70, 70})); + connect(materialstream2.Out, streammixer.In) annotation( + Line(points = {{0, 18}, {40, 18}, {40, -4}}, color = {0, 70, 70})); + connect(materialstream3.Out, streammixer.In) annotation( + Line(points = {{12, -26}, {40, -26}, {40, -4}}, color = {0, 70, 70})); + connect(streammixer.Out, materialstream4.In) annotation( + Line(points = {{60, -4}, {90, -4}, {90, -24}}, color = {0, 70, 70})); + connect(materialstream4.Out, Separator.In) annotation( + Line(points = {{110, -24}, {146, -24}, {146, -6}}, color = {0, 70, 70})); + connect(Separator.Out, materialstream5.In) annotation( + Line(points = {{166, -6}, {210, -6}, {210, 4}}, color = {0, 70, 70})); + connect(Separator.Out, materialstream6.In) annotation( + Line(points = {{166, -6}, {198, -6}, {198, -34}, {206, -34}}, color = {0, 70, 70})); + connect(energystream1.Out, Separator.energy) annotation( + Line(points = {{140, -62}, {156, -62}, {156, -18}}, color = {255, 0, 0})); + connect(materialstream6.Out, recycleblock.inlet) annotation( + Line(points = {{226, -34}, {260, -34}, {260, -58}}, color = {0, 70, 70})); + connect(recycleblock.outlet, materialstream.In) annotation( + Line(points = {{280, -58}, {318, -58}, {318, -124}, {-306, -124}, {-306, -80}, {-270, -80}}, color = {0, 70, 70})); + +end methanol; + + +end Formaldehyde_987; diff --git a/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/README.txt b/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/README.txt new file mode 100644 index 0000000..6ee0c91 --- /dev/null +++ b/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Vapor Compression Refrigeration Cycle +Proposar Name: Ms Yutika Naik +University: Sardar Vallabhbhai National Institute of Technology, Surat + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/abstract.pdf b/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/abstract.pdf new file mode 100644 index 0000000..c855985 Binary files /dev/null and b/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/abstract.pdf differ diff --git a/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/flowsheet.mo b/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/flowsheet.mo new file mode 100644 index 0000000..5779f3f --- /dev/null +++ b/Vapor_Compression_Refrigeration_Cycle_By_Ms_Yutika_Naik/flowsheet.mo @@ -0,0 +1,76 @@ +package Vaporcompression +model MS "Extension of Material Stream with Raoult's Law" + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "This is a non-executable model is created inside the package Heater to extend the MaterialStream model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the HeaterSimulation model to create the required number of instances of the material stream model.
")); +end MS; +model AdiabComp "Extension of Adiabatic Compressor with Raoult's Law" + extends Simulator.UnitOperations.AdiabaticCompressor; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; +annotation( + Documentation(info = "This is a non-executable model is created inside the package Compressor to extend the AdiabaticCompressor model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the CompressorSimulation model to create the required number of instances of the adiabatic compressor model.
")); +end AdiabComp; + +model flowsheet +import data = Simulator.Files.ChemsepDatabase; + parameter data.Propane prop; + parameter Integer Nc = 1; + parameter data.GeneralProperties C[Nc] = {prop}; + Vaporcompression.MS S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-130, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Vaporcompression.MS S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-70, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-90, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Vaporcompression.AdiabComp compressor(C = C, Eff = 1, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-100, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler(C = C, Eff = 1, Nc = Nc, Pdel = 0.00) annotation( + Placement(visible = true, transformation(origin = {-40, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {-20, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Vaporcompression.MS S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-10, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve valve(C = C, Fg = 1, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {20, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Vaporcompression.MS S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {50, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater evaporator(C = C, Eff = 1.00, Nc = Nc, Pdel = 0.00) annotation( + Placement(visible = true, transformation(origin = {79, 21}, extent = {{-9, -9}, {9, 9}}, rotation = 0))); + Vaporcompression.MS S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {110, 20}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E3 annotation( + Placement(visible = true, transformation(origin = {80, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S1.x_pc[1, :] = {1}; + S1.P = 101325; + S1.T = 230.945240; + S1.F_p[1] = 22.677280; + S2.P = 960000.0; + S3.T = 298.149230; + S4.P = 101325.00; + S5.T = 230.945240; + connect(S1.Out, compressor.In) annotation( + Line(points = {{-120, 20}, {-110, 20}}, color = {0, 70, 70})); + connect(compressor.Out, S2.In) annotation( + Line(points = {{-90, 20}, {-80, 20}}, color = {0, 70, 70})); + connect(S2.Out, cooler.In) annotation( + Line(points = {{-60, 20}, {-50, 20}}, color = {0, 70, 70})); + connect(cooler.Out, S3.In) annotation( + Line(points = {{-30, 20}, {-20, 20}}, color = {0, 70, 70})); + connect(S3.Out, valve.In) annotation( + Line(points = {{0, 20}, {10, 20}}, color = {0, 70, 70})); + connect(valve.Out, S4.In) annotation( + Line(points = {{30, 20}, {40, 20}}, color = {0, 70, 70})); + connect(S4.Out, evaporator.In) annotation( + Line(points = {{60, 20}, {60, 20.5}, {70, 20.5}, {70, 21}}, color = {0, 70, 70})); + connect(compressor.En, E1.In) annotation( + Line(points = {{-100, 13}, {-100, 0}}, color = {255, 0, 0})); + connect(cooler.En, E2.In) annotation( + Line(points = {{-30, 10}, {-30, 0}}, color = {255, 0, 0})); + connect(evaporator.En, E3.In) annotation( + Line(points = {{70, 12}, {70, 0}}, color = {255, 0, 0})); + connect(evaporator.Out, S5.In) annotation( + Line(points = {{88, 20}, {100, 20}, {100, 20}, {100, 20}}, color = {0, 70, 70})); + end flowsheet; +end Vaporcompression; diff --git a/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/README.txt b/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/README.txt new file mode 100644 index 0000000..8fad492 --- /dev/null +++ b/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Water Gas Shift Reaction for Production of Hydrogen +Proposar Name: Ms Naik Yutika Niralkumar +University: Sardar Vallabhbhai National Institute of Technology, Surat + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/Watergasshiftreactionabstract.pdf b/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/Watergasshiftreactionabstract.pdf new file mode 100644 index 0000000..f33cb99 Binary files /dev/null and b/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/Watergasshiftreactionabstract.pdf differ diff --git a/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/watergasshiftreactionfinal.mo b/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/watergasshiftreactionfinal.mo new file mode 100644 index 0000000..ab0d4f8 --- /dev/null +++ b/Water_Gas_Shift_Reaction_For_Production_Of_Hydrogen_By_Ms_Naik_Yutika_Niralkumar/watergasshiftreactionfinal.mo @@ -0,0 +1,102 @@ +package watergasshiftreactionfinal + + model MS "Extending Material Stream with Raoult's Law" + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "
This is a non-executable model is created inside the package Mixer to extend the MaterialStream model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the MixerSimulation model to create the required number of instances of the material stream model.
")); + end MS; + + model ConvReactor "Extension of Conversion Reactor with Conversion Reaction" + extends Simulator.UnitOperations.ConversionReactor; + extends Simulator.Files.Models.ReactionManager.ConversionReaction; + annotation( + Documentation(info = "This is a non-executable model is created inside the package CR to extend the ConversionReactor model along with the necessary reaction from Reaction Manager which is ConversionReaction in this case.

It will be instantiated in the ConvReactSimulation model to create the required number of instances of the adiabatic expander model.
")); + end ConvReactor; + + model FlashSep "Extension of Flash Separator with Raoult's Law" + extends Simulator.UnitOperations.Flash; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + annotation( + Documentation(info = "This is a non-executable model is created inside the package Flash to extend the FlashColumn model along with the necessary property method from ThermodynamicPackages which is RaoultsLaw in this case.

It will be instantiated in the FlashSimulation model to create the required instance of the flash column model.
")); + end FlashSep; + + model flowsheet + parameter Integer Nc = 4; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Carbonmonoxide cm; + parameter data.Carbondioxide cd; + parameter data.Hydrogen hn; + parameter data.Water wtr; + parameter data.GeneralProperties C[Nc] = {cm, cd, hn, wtr}; + watergasshiftreactionfinal.MS S1(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-126, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Mixer mixer(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Average") annotation( + Placement(visible = true, transformation(origin = {-94, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S2(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-126, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S3(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-66, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S4(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-6, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-54, -26}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler(C = C, Eff = 1, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {24, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S5(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {56, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {50, -12}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S6(C = C, Fg = 10, Nc = Nc, x_pc(fixed = false)) annotation( + Placement(visible = true, transformation(origin = {116, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S7(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {116, -10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.ConvReactor cr1(BC_r = {1}, C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{-1}, {1}, {1}, {-1}}, Nc = Nc, Nr = 1, Pdel = 0, Tdef = 742.8, X_r = {0.80056}) annotation( + Placement(visible = true, transformation(origin = {-36, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.FlashSep flashSep(BTdef = false, C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {86, -2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Cooler cooler1(C = C, Eff = 1, Fg = 24, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {144, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + watergasshiftreactionfinal.MS S8(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {172, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S1.P = 101320; + S2.P = 101325; + S1.T = 298.15; + S2.T = 373.15; + S1.F_p[1] = 15.278; + S2.F_p[1] = 19.444; + S1.x_pc[1, :] = {1, 0, 0, 0}; + S2.x_pc[1, :] = {0, 0, 0, 1}; + S5.T = 70;//32.8; + S8.T = 20.4857; + connect(S1.Out, mixer.In[1]) annotation( + Line(points = {{-116, 2}, {-104, 2}, {-104, -2}}, color = {0, 70, 70})); + connect(S2.Out, mixer.In[2]) annotation( + Line(points = {{-116, -2}, {-104, -2}}, color = {0, 70, 70})); + connect(mixer.Out, S3.In) annotation( + Line(points = {{-84, -2}, {-76, -2}}, color = {0, 70, 70})); + connect(S4.Out, cooler.In) annotation( + Line(points = {{4, -2}, {14, -2}}, color = {0, 70, 70})); + connect(cooler.Out, S5.In) annotation( + Line(points = {{34, -2}, {46, -2}}, color = {0, 70, 70})); + connect(cooler.En, E2.In) annotation( + Line(points = {{34, -12}, {40, -12}}, color = {255, 0, 0})); + connect(S3.Out, cr1.In) annotation( + Line(points = {{-56, -2}, {-46, -2}}, color = {0, 70, 70})); + connect(cr1.Out, S4.In) annotation( + Line(points = {{-26, -2}, {-16, -2}}, color = {0, 70, 70})); + connect(E1.Out, cr1.energy) annotation( + Line(points = {{-44, -26}, {-36, -26}, {-36, -15}}, color = {255, 0, 0})); + connect(S6.Out, cooler1.In) annotation( + Line(points = {{126, 6}, {134, 6}}, color = {0, 70, 70})); + connect(cooler1.Out, S8.In) annotation( + Line(points = {{154, 6}, {162, 6}}, color = {0, 70, 70})); + connect(S5.Out, flashSep.In) annotation( + Line(points = {{66, -2}, {76, -2}}, color = {0, 70, 70})); + connect(flashSep.Out2, S7.In) annotation( + Line(points = {{96, -10}, {106, -10}}, color = {0, 70, 70})); + connect(flashSep.Out1, S6.In) annotation( + Line(points = {{96, 6}, {106, 6}}, color = {0, 70, 70})); + end flowsheet; +end watergasshiftreactionfinal; diff --git a/_Pressure-Swing_Distillation_For_Isopropyl_Alcohol_And_Diisopropyl_Ether_Separation_By_Mr_Krishna_Patel/Abstract.pdf b/_Pressure-Swing_Distillation_For_Isopropyl_Alcohol_And_Diisopropyl_Ether_Separation_By_Mr_Krishna_Patel/Abstract.pdf new file mode 100644 index 0000000..376f49d Binary files /dev/null and b/_Pressure-Swing_Distillation_For_Isopropyl_Alcohol_And_Diisopropyl_Ether_Separation_By_Mr_Krishna_Patel/Abstract.pdf differ diff --git a/_Pressure-Swing_Distillation_For_Isopropyl_Alcohol_And_Diisopropyl_Ether_Separation_By_Mr_Krishna_Patel/Flowsheet.mo b/_Pressure-Swing_Distillation_For_Isopropyl_Alcohol_And_Diisopropyl_Ether_Separation_By_Mr_Krishna_Patel/Flowsheet.mo new file mode 100644 index 0000000..5149c94 --- /dev/null +++ b/_Pressure-Swing_Distillation_For_Isopropyl_Alcohol_And_Diisopropyl_Ether_Separation_By_Mr_Krishna_Patel/Flowsheet.mo @@ -0,0 +1,116 @@ +package PSD + +//model for Material_Stream + + model MS + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end MS; + +//model for Distillation Column + + package Distillation_Column + model Condenser + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Condenser; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Reboiler; + + model DC + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condenser condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end DC; + end Distillation_Column; + +//model for flowsheet + + model flowsheet + + extends Modelica.Icons.Example; + import data = Simulator.Files.ChemsepDatabase; + parameter data.Diisopropylether DIPE; + parameter data.Isopropanol IPA; + parameter Integer Nc = 2; + parameter Simulator.Files.ChemsepDatabase.GeneralProperties C[Nc] = {DIPE, IPA}; + PSD.MS Feed(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-168, 30}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MS Recycle(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-168, -10}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.Distillation_Column.DC HPC(C = C, Ctype = "Total", InT_s = {6, 13}, Nc = Nc, Ni = 2, Nt = 38) annotation( + Placement(visible = true, transformation(origin = {-112, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E1 annotation( + Placement(visible = true, transformation(origin = {-70, 74}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E2 annotation( + Placement(visible = true, transformation(origin = {-76, -72}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MS HPC_top(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-56, 34}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MS HPC_bottom(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-54, -36}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Valve valve(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-20, 22}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MS LPC_feed(C = C, Fg = 28.36, Nc = Nc, Pg = 101325) annotation( + Placement(visible = true, transformation(origin = {12, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.Distillation_Column.DC LPC(C = C, Ctype = "Total", InT_s = {3}, Nc = Nc, Ni = 1, Nt = 18) annotation( + Placement(visible = true, transformation(origin = {56, 2}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MS LPC_top(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {108, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MS LPC_bottom(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {114, -28}, extent = {{10, -10}, {-10, 10}}, rotation = 180))); + + equation + + connect(Feed.Out, HPC.In_s[1]) annotation( + Line(points = {{-158, 30}, {-137, 30}, {-137, 4}}, color = {0, 70, 70})); + connect(Recycle.Out, HPC.In_s[2]) annotation( + Line(points = {{-158, -10}, {-137, -10}, {-137, 4}}, color = {0, 70, 70})); + connect(HPC.Cduty, E1.In) annotation( + Line(points = {{-86, 64}, {-80, 64}, {-80, 74}, {-80, 74}}, color = {255, 0, 0})); + connect(HPC.Rduty, E2.In) annotation( + Line(points = {{-86, -56}, {-86, -72}}, color = {255, 0, 0})); + connect(HPC.Dist, HPC_top.In) annotation( + Line(points = {{-86, 34}, {-66, 34}, {-66, 34}, {-66, 34}}, color = {0, 70, 70})); + connect(HPC.Bot, HPC_bottom.In) annotation( + Line(points = {{-86, -26}, {-70, -26}, {-70, -36}, {-64, -36}}, color = {0, 70, 70})); + connect(HPC_top.Out, valve.In) annotation( + Line(points = {{-46, 34}, {-39, 34}, {-39, 22}, {-30, 22}}, color = {0, 70, 70})); + connect(valve.Out, LPC_feed.In) annotation( + Line(points = {{-10, 22}, {1, 22}, {1, 2}, {2, 2}}, color = {0, 70, 70})); + connect(LPC_feed.Out, LPC.In_s[1]) annotation( + Line(points = {{22, 2}, {31, 2}}, color = {0, 70, 70})); + connect(LPC.Dist, LPC_top.In) annotation( + Line(points = {{81, 32}, {98, 32}}, color = {0, 70, 70})); + connect(LPC.Bot, LPC_bottom.In) annotation( + Line(points = {{81, -28}, {104, -28}}, color = {0, 70, 70})); + + Feed.P = 1013250; + Feed.T = 298.15; + Feed.F_p[1] = 27.78; + Feed.x_pc[1, :] = {0.75, 0.25}; + Recycle.P = 1013250; + Recycle.T = 340; + Recycle.F_p[1] = 21.58; + Recycle.x_pc[1, :] = {0.7550, 0.2450}; + HPC.condenser.P = 1013250; + HPC.reboiler.P = 1013250; + HPC.RR = 5; + HPC_bottom.F_p[1] = 20.99; + valve.Pout = 101325; + LPC.condenser.P = 101325; + LPC.reboiler.P = 101325; + LPC.RR = 4; + LPC_top.F_p[1] = 21.58; + + end flowsheet; + +end PSD; diff --git a/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/Abstract_WC.pdf b/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/Abstract_WC.pdf new file mode 100644 index 0000000..3d3b1a6 Binary files /dev/null and b/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/Abstract_WC.pdf differ diff --git a/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/PSD.mo b/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/PSD.mo new file mode 100644 index 0000000..47c8747 --- /dev/null +++ b/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/PSD.mo @@ -0,0 +1,98 @@ +package PSD + model MSTR + extends Simulator.Streams.MaterialStream; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end MSTR; + + package rigDist + model Condensor + extends Simulator.UnitOperations.DistillationColumn.Cond; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Condensor; + + model Tray + extends Simulator.UnitOperations.DistillationColumn.DistTray; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Tray; + + model Reboiler + extends Simulator.UnitOperations.DistillationColumn.Reb; + extends Simulator.Files.ThermodynamicPackages.RaoultsLaw; + end Reboiler; + + model DistColumn + extends Simulator.UnitOperations.DistillationColumn.DistCol; + Condensor condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]); + Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]); + Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]); + end DistColumn; + end rigDist; + + model Flowsheet + import data = Simulator.Files.ChemsepDatabase; + parameter data.Water wat; + parameter data.Cyclohexane cyh; + parameter Integer Nc = 2; + parameter data.GeneralProperties C[Nc] = {wat, cyh}; + PSD.MSTR S01(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-130, 24}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S02(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-130, -6}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.rigDist.DistColumn DC01(C = C, Ctype = "Total", InT_s = {3, 7}, Nc = Nc, Ni = 2, Nt = 18) annotation( + Placement(visible = true, transformation(origin = {-50, 8}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S03(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {-16, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S04(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {2, -60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.UnitOperations.Heater Heater(C = C, Eff = 0.75, Nc = Nc, Pdel = 0) annotation( + Placement(visible = true, transformation(origin = {24, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S05(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {64, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.rigDist.DistColumn DC02(C = C, Ctype = "Total", InT_s = {21}, Nc = Nc, Ni = 1, Nt = 40) annotation( + Placement(visible = true, transformation(origin = {120, 8}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S06(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {158, 38}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + PSD.MSTR S07(C = C, Nc = Nc) annotation( + Placement(visible = true, transformation(origin = {170, -60}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + Simulator.Streams.EnergyStream E01 annotation( + Placement(visible = true, transformation(origin = {4, 4}, extent = {{-10, -10}, {10, 10}}, rotation = 0))); + equation + S01.P = 101325; + S01.T = 342.424; + S01.F_p[1] = 277.778; + S01.x_pc[1,:] = {0.70, 0.3}; + S02.P = 101325; + S02.T = 342.075; + S02.F_p[1] = 120.508; + S02.x_pc[1,:] = {0.73, 0.27}; + DC01.condenser.P = 101325; + DC01.reboiler.P = 101325; + DC01.RR = 2; + S04.x_pc[1,1] = 0.99; + S05.T = 450; + DC02.condenser.P = 303975; + DC02.reboiler.P = 303975; + DC02.RR = 10; + S07.F_p[1] = 120.44; + connect(S01.Out, DC01.In_s[1]) annotation( + Line(points = {{-120, 24}, {-96, 24}, {-96, 8}, {-75, 8}}, color = {0, 70, 70})); + connect(S02.Out, DC01.In_s[2]) annotation( + Line(points = {{-120, -6}, {-96, -6}, {-96, 8}, {-75, 8}}, color = {0, 70, 70})); + connect(DC01.Dist, S03.In) annotation( + Line(points = {{-24, 38}, {-26, 38}}, color = {0, 70, 70})); + connect(DC01.Bot, S04.In) annotation( + Line(points = {{-24, -22}, {-8, -22}, {-8, -60}}, color = {0, 70, 70})); + connect(S03.Out, Heater.In) annotation( + Line(points = {{-6, 38}, {14, 38}, {14, 38}, {14, 38}}, color = {0, 70, 70})); + connect(Heater.Out, S05.In) annotation( + Line(points = {{34, 38}, {54, 38}, {54, 38}, {54, 38}}, color = {0, 70, 70})); + connect(S05.Out, DC02.In_s[1]) annotation( + Line(points = {{74, 38}, {83.5, 38}, {83.5, 8}, {95, 8}}, color = {0, 70, 70})); + connect(DC02.Bot, S07.In) annotation( + Line(points = {{146, -22}, {160, -22}, {160, -60}}, color = {0, 70, 70})); + connect(DC02.Dist, S06.In) annotation( + Line(points = {{146, 38}, {148, 38}}, color = {0, 70, 70})); + connect(E01.Out, Heater.En) annotation( + Line(points = {{14, 4}, {14, 28}}, color = {255, 0, 0})); + end Flowsheet; +end PSD; diff --git a/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/README.txt b/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/README.txt new file mode 100644 index 0000000..020e4fd --- /dev/null +++ b/_Pressure_Swing_Distillation_For_Separation_Of_Water_And_Cyclohexane_By_Mr_Ali_Asger/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Pressure Swing Distillation for Separation of Water and Cyclohexane +Proposar Name: Mr Ali Asger +University: Institute of Chemical Technology, Mumbai Off-Campus Marathwada, Jalna + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay diff --git a/zip-1559634800-567987.zip b/zip-1559634800-567987.zip deleted file mode 100755 index 891b01f..0000000 Binary files a/zip-1559634800-567987.zip and /dev/null differ diff --git a/zip-1572330485-226364.zip b/zip-1572330485-226364.zip deleted file mode 100755 index ebdd195..0000000 Binary files a/zip-1572330485-226364.zip and /dev/null differ diff --git a/zip-1572330485-302807.zip b/zip-1572330485-302807.zip deleted file mode 100755 index ebdd195..0000000 Binary files a/zip-1572330485-302807.zip and /dev/null differ -- cgit