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RahulNagraj444RahulNagraj444
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Merge pull request #48 from nayakpriyam/master
Added Test Examples Documentation and Modified Model Documentation
2 parents 26a5754 + 9ebb12a commit a8957fa

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‎Sample_Flowsheets/Acetic_Acid_Esterification.mo‎

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package Acetic_Acid_Esterification
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model ms
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extends Simulator.Streams.MaterialStream;
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extends Simulator.Files.ThermodynamicPackages.NRTL;
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end ms;
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model Fls
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extends Simulator.UnitOperations.Flash;
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extends Simulator.Files.ThermodynamicPackages.NRTL;
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end Fls;
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model Conv_React
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extends Simulator.UnitOperations.ConversionReactor;
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extends Simulator.Files.Models.ReactionManager.ConversionReaction;
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end Conv_React;
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model Flowsheet
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import data = Simulator.Files.ChemsepDatabase;
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parameter Integer Nc = 4;
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parameter data.Ethylacetate etac;
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parameter data.Water wat;
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parameter data.Aceticacid aa;
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parameter data.Ethanol eth;
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parameter data.GeneralProperties C[Nc] = {etac, wat, aa, eth};
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Simulator.UnitOperations.Mixer MIX_01(C = C, NI = 3, Nc = Nc, outPress = "Inlet_Average") annotation(
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Placement(visible = true, transformation(origin = {-48, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Acetic_Acid_Esterification.Conv_React CR_01(BC_r = {3},C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{1}, {1}, {-1}, {-1}}, Nc = Nc, Nr = 1, Tdef = 300, X_r = {0.6}) annotation(
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Placement(visible = true, transformation(origin = {16, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Simulator.UnitOperations.Splitter SPLIT_01(C = C, CalcType = "Split_Ratio", Nc = Nc, No = 2) annotation(
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Placement(visible = true, transformation(origin = {82, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Acetic_Acid_Esterification.ms S_01(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-88, 26}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Acetic_Acid_Esterification.ms S_02(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-88, -30}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Acetic_Acid_Esterification.ms S_03(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-18, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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ms S_04(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {48, 0}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Acetic_Acid_Esterification.ms S_05(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {116, 24}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Acetic_Acid_Esterification.ms S_06(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {116, -28}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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equation
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connect(S_05.Out, MIX_01.inlet[3]) annotation(
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Line(points = {{126, 24}, {140, 24}, {140, 50}, {-114, 50}, {-114, 0}, {-58, 0}, {-58, 0}}, color = {0, 70, 70}));
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connect(SPLIT_01.Out[1], S_05.In) annotation(
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Line(points = {{92, 0}, {106, 0}, {106, 24}}, color = {0, 70, 70}));
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connect(SPLIT_01.Out[2], S_06.In) annotation(
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Line(points = {{92, 0}, {106, 0}, {106, -28}}, color = {0, 70, 70}));
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connect(S_04.Out, SPLIT_01.In) annotation(
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Line(points = {{58, 0}, {72, 0}, {72, 0}, {72, 0}}, color = {0, 70, 70}));
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connect(CR_01.Out, S_04.In) annotation(
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Line(points = {{26, 0}, {38, 0}, {38, 0}, {38, 0}}, color = {0, 70, 70}));
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connect(S_03.Out, CR_01.In) annotation(
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Line(points = {{-8, 0}, {6, 0}, {6, 0}, {6, 0}}, color = {0, 70, 70}));
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connect(MIX_01.outlet, S_03.In) annotation(
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Line(points = {{-38, 0}, {-28, 0}, {-28, 0}, {-28, 0}}, color = {0, 70, 70}));
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connect(S_02.Out, MIX_01.inlet[2]) annotation(
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Line(points = {{-78, -30}, {-58, -30}, {-58, 0}, {-58, 0}}, color = {0, 70, 70}));
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connect(S_01.Out, MIX_01.inlet[1]) annotation(
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Line(points = {{-78, 26}, {-58, 26}, {-58, 0}, {-58, 0}}, color = {0, 70, 70}));
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S_01.P = 101325;
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S_01.T = 300;
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S_01.x_pc[1, :] = {0, 0, 0, 1};
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S_01.F_p[1] = 60;
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S_02.P = 101325;
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S_02.T = 300;
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S_02.x_pc[1, :] = {0, 0, 1, 0};
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S_02.F_p[1] = 40;
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SPLIT_01.SpecVal_s = {0.75, 0.25};
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end Flowsheet;
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end Acetic_Acid_Esterification;

‎Sample_Flowsheets/Acetic_Acid_Esterification_by_Ethanol.mo‎

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This file was deleted.

‎Sample_Flowsheets/DiethylEther_from_Ethanol.mo‎

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package DiethylEther_from_Ethanol
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model ms
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extends Simulator.Streams.MaterialStream;
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extends Simulator.Files.ThermodynamicPackages.RaoultsLaw;
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end ms;
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model CR
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extends Simulator.UnitOperations.ConversionReactor;
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extends Simulator.Files.Models.ReactionManager.ConversionReaction;
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end CR;
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package rigDist
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model Condenser
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extends Simulator.UnitOperations.DistillationColumn.Cond;
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extends Simulator.Files.ThermodynamicPackages.RaoultsLaw;
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end Condenser;
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model Tray
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extends Simulator.UnitOperations.DistillationColumn.DistTray;
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extends Simulator.Files.ThermodynamicPackages.RaoultsLaw;
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end Tray;
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model Reboiler
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extends Simulator.UnitOperations.DistillationColumn.Reb;
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extends Simulator.Files.ThermodynamicPackages.RaoultsLaw;
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end Reboiler;
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model DistColumn
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extends Simulator.UnitOperations.DistillationColumn.DistCol;
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Condenser condenser(Nc = Nc, C = C, Ctype = Ctype, Bin = Bin_t[1]);
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Reboiler reboiler(Nc = Nc, C = C, Bin = Bin_t[Nt]);
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Tray tray[Nt - 2](each Nc = Nc, each C = C, Bin = Bin_t[2:Nt - 1]);
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end DistColumn;
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end rigDist;
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model Flowsheet
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import data = Simulator.Files.ChemsepDatabase;
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parameter data.Diethylether dieth;
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parameter data.Ethanol eth;
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parameter data.Water wat;
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parameter Integer Nc = 3;
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parameter data.GeneralProperties C[Nc] = {dieth, eth, wat};
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Simulator.UnitOperations.Mixer MIX_01(C = C, NI = 2, Nc = Nc, outPress = "Inlet_Average") annotation(
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Placement(visible = true, transformation(origin = {-48, 48}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.CR REACT_01(BC_r = {2}, C = C, CalcMode = "Define_Out_Temperature", Coef_cr = {{1}, {-2}, {1}}, Nc = Nc, Nr = 1, Tdef = 298.15, X_r = {0.5}) annotation(
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Placement(visible = true, transformation(origin = {38, 50}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.rigDist.DistColumn DC_01(C = C, Ctype = "Total", InT_s = {4}, Nc = Nc, Ni = 1, Nt = 8) annotation(
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Placement(visible = true, transformation(origin = {66, -38}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.rigDist.DistColumn DC_02(C = C, Ctype = "Total", InT_s = {7}, Nc = Nc, Ni = 1, Nt = 10) annotation(
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Placement(visible = true, transformation(origin = {-48, -38}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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ms S_01(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-84, 66}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.ms S_02(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-86, 40}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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ms S_03(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-8, 50}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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ms S_04(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {80, 50}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.ms S_05(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {10, -4}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.ms S_06(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {8, -70}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.ms S_07(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-106, -8}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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DiethylEther_from_Ethanol.ms S_08(C = C, Nc = Nc) annotation(
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Placement(visible = true, transformation(origin = {-106, -66}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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Simulator.Streams.EnergyStream E_01 annotation(
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Placement(visible = true, transformation(origin = {20, 8}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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Simulator.Streams.EnergyStream E_02 annotation(
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Placement(visible = true, transformation(origin = {18, -98}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Simulator.Streams.EnergyStream E_03 annotation(
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Placement(visible = true, transformation(origin = {10, 28}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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Simulator.Streams.EnergyStream E_04 annotation(
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Placement(visible = true, transformation(origin = {-92, 22}, extent = {{10, -10}, {-10, 10}}, rotation = 0)));
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Simulator.Streams.EnergyStream E_05 annotation(
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Placement(visible = true, transformation(origin = {-106, -98}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
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equation
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connect(S_06.Out, DC_02.In_s[1]) annotation(
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Line(points = {{-2, -70}, {-6, -70}, {-6, -38}, {-22, -38}, {-22, -38}}, color = {0, 70, 70}));
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connect(E_05.Out, DC_02.Rduty) annotation(
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Line(points = {{-96, -98}, {-74, -98}, {-74, -98}, {-72, -98}}, color = {255, 0, 0}));
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connect(E_02.Out, DC_01.Rduty) annotation(
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Line(points = {{28, -98}, {40, -98}, {40, -98}, {42, -98}}, color = {255, 0, 0}));
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connect(DC_02.Cduty, E_04.In) annotation(
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Line(points = {{-72, 22}, {-82, 22}}, color = {255, 0, 0}));
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connect(DC_01.Cduty, E_01.In) annotation(
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Line(points = {{42, 22}, {30, 22}, {30, 8}, {30, 8}}, color = {255, 0, 0}));
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connect(E_03.Out, REACT_01.energy) annotation(
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Line(points = {{20, 28}, {38, 28}, {38, 38}, {38, 38}}, color = {255, 0, 0}));
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connect(S_08.In, DC_02.Bot) annotation(
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Line(points = {{-96, -66}, {-72, -66}, {-72, -68}, {-74, -68}, {-74, -68}}, color = {0, 70, 70}));
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connect(S_07.In, DC_02.Dist) annotation(
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Line(points = {{-96, -8}, {-72, -8}, {-72, -8}, {-72, -8}}, color = {0, 70, 70}));
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connect(S_06.In, DC_01.Bot) annotation(
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Line(points = {{18, -70}, {40, -70}, {40, -68}, {40, -68}}, color = {0, 70, 70}));
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connect(S_05.In, DC_01.Dist) annotation(
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Line(points = {{20, -4}, {40, -4}, {40, -8}, {42, -8}}, color = {0, 70, 70}));
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connect(S_04.Out, DC_01.In_s[1]) annotation(
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Line(points = {{90, 50}, {128, 50}, {128, -38}, {92, -38}, {92, -38}}, color = {0, 70, 70}));
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connect(REACT_01.Out, S_04.In) annotation(
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Line(points = {{48, 50}, {70, 50}, {70, 50}, {70, 50}}, color = {0, 70, 70}));
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connect(S_03.Out, REACT_01.In) annotation(
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Line(points = {{2, 50}, {28, 50}, {28, 50}, {28, 50}, {28, 50}}, color = {0, 70, 70}));
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connect(MIX_01.outlet, S_03.In) annotation(
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Line(points = {{-38, 48}, {-18, 48}, {-18, 50}, {-18, 50}}, color = {0, 70, 70}));
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connect(S_02.Out, MIX_01.inlet[2]) annotation(
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Line(points = {{-76, 40}, {-64, 40}, {-64, 48}, {-58, 48}, {-58, 48}}, color = {0, 70, 70}));
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connect(S_01.Out, MIX_01.inlet[1]) annotation(
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Line(points = {{-74, 66}, {-64, 66}, {-64, 48}, {-58, 48}, {-58, 48}}, color = {0, 70, 70}));
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S_01.T = 347.602;
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S_01.P = 101325;
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S_01.F_p[1] = 20.7564;
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S_01.x_pc[1, :] = {0.025052486, 0.81126839, 0.16367913};
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S_02.T = 313.15;
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S_02.P = 101325;
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S_02.F_p[1] = 20;
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S_02.x_pc[1, :] = {0, 0.85, 0.15};
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DC_01.condenser.P = 101325;
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DC_01.reboiler.P = 101325;
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DC_01.RR = 3;
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S_06.F_p[1] = 30.7662;
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DC_02.condenser.P = 101325;
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DC_02.reboiler.P = 101325;
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DC_02.RR = 2;
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S_08.F_p[1] = 14.7189;
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end Flowsheet;
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end DiethylEther_from_Ethanol;

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