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-rw-r--r--Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Abstract.pdfbin0 -> 57803 bytes
-rw-r--r--Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Flowsheet_PSDWater.mo147
-rw-r--r--Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/README.txt8
3 files changed, 155 insertions, 0 deletions
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
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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
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+++ b/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/Flowsheet_PSDWater.mo
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+package Pres_swin_Dist
+ model Material_Streams
+ //instantiation of chemsep database
+ import data = Simulator.Files.Chemsep_Database;
+ //instantiation of Ethanol
+ parameter data.Ethanol eth;
+ //instantiation of Water
+ parameter data.Water wat;
+ extends Simulator.Streams.Material_Stream(NOC = 2, comp = {eth, wat}, totMolFlo(each start = 1), compMolFrac(each start = 0.5), 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 NRTL is extended
+ end Material_Streams;
+
+ model flowsheet
+ import data = Simulator.Files.Chemsep_Database;
+ //instantiation of Ethanol
+ parameter data.Ethanol eth;
+ //instantiation of Water
+ parameter data.Water wat;
+ //Number of Components
+ parameter Integer NOC = 2;
+ parameter data.General_Properties comp[NOC] = {eth, wat};
+ Pres_swin_Dist.LPC.DistColumn LPC(NOC = NOC, comp = comp, feedStages = {5, 16}, noOfFeeds = 2, noOfStages = 22) annotation(
+ Placement(visible = true, transformation(origin = {-40, 8}, extent = {{-28, -28}, {28, 28}}, rotation = 0)));
+ Pres_swin_Dist.Material_Streams Distillate1(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {8, 58}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Pres_swin_Dist.Material_Streams Bottoms1(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {10, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Simulator.Streams.Energy_Stream C_duty1 annotation(
+ Placement(visible = true, transformation(origin = {-30, 70}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Simulator.Streams.Energy_Stream R_duty1 annotation(
+ Placement(visible = true, transformation(origin = {-30, -50}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Pres_swin_Dist.HPC.DistColumn HPC(NOC = NOC, comp = comp, feedStages = {7}, noOfFeeds = 1, noOfStages = 22) annotation(
+ Placement(visible = true, transformation(origin = {62, 8}, extent = {{-28, -28}, {28, 28}}, rotation = 0)));
+ Material_Streams Distillate2(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {118, 58}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Material_Streams Bottoms2(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {122, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Simulator.Streams.Energy_Stream C_duty2 annotation(
+ Placement(visible = true, transformation(origin = {74, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Simulator.Streams.Energy_Stream R_duty2 annotation(
+ Placement(visible = true, transformation(origin = {76, -50}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Material_Streams Feed(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {-104, -12}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Material_Streams Recycle(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {-102, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Simulator.Unit_Operations.Cooler cooler1(pressDrop = 0, eff = 1, NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {166, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Material_Streams material_Streams1(NOC = NOC, comp = comp) annotation(
+ Placement(visible = true, transformation(origin = {214, -38}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ equation
+ connect(cooler1.outlet, material_Streams1.inlet) annotation(
+ Line(points = {{176, -38}, {204, -38}, {204, -38}, {204, -38}}));
+ connect(Bottoms2.outlet, cooler1.inlet) annotation(
+ Line(points = {{132, -38}, {156, -38}}));
+ connect(Recycle.outlet, LPC.feed[2]) annotation(
+ Line(points = {{-92, 32}, {-68, 32}, {-68, 8}, {-68, 8}, {-68, 6}}));
+ connect(Feed.outlet, LPC.feed[1]) annotation(
+ Line(points = {{-94, -12}, {-80, -12}, {-80, 8}, {-66, 8}, {-66, 6}, {-68, 6}}));
+ connect(Bottoms1.outlet, HPC.feed[1]) annotation(
+ Line(points = {{20, -38}, {24, -38}, {24, 6}, {34, 6}, {34, 6}}));
+ connect(Bottoms2.inlet, HPC.bottoms) annotation(
+ Line(points = {{112, -38}, {104, -38}, {104, -12}, {90, -12}, {90, -12}, {90, -12}}));
+ connect(Distillate2.inlet, HPC.distillate) annotation(
+ Line(points = {{108, 58}, {100, 58}, {100, 28}, {90, 28}, {90, 28}, {90, 28}}));
+ connect(R_duty2.inlet, HPC.reboiler_duty) annotation(
+ Line(points = {{66, -50}, {56, -50}, {56, -34}, {82, -34}, {82, -22}, {82, -22}, {82, -20}}));
+ connect(C_duty2.inlet, HPC.condensor_duty) annotation(
+ Line(points = {{64, 68}, {58, 68}, {58, 42}, {78, 42}, {78, 34}, {78, 34}, {78, 34}}));
+ connect(Bottoms1.inlet, LPC.bottoms) annotation(
+ Line(points = {{0, -38}, {-4, -38}, {-4, -12}, {-12, -12}, {-12, -12}, {-12, -12}}));
+ connect(Distillate1.inlet, LPC.distillate) annotation(
+ Line(points = {{-2, 58}, {-8, 58}, {-8, 28}, {-12, 28}, {-12, 28}, {-12, 28}}));
+ connect(C_duty1.inlet, LPC.condensor_duty) annotation(
+ Line(points = {{-40, 70}, {-48, 70}, {-48, 50}, {-24, 50}, {-24, 34}, {-24, 34}}));
+ connect(R_duty1.inlet, LPC.reboiler_duty) annotation(
+ Line(points = {{-40, -50}, {-48, -50}, {-48, -32}, {-20, -32}, {-20, -22}, {-20, -22}, {-20, -20}}));
+ Feed.compMolFrac[1, :] = {0.3, 0.7};
+ Feed.T = 348.15;
+ Feed.totMolFlo[1] = 27.7778;
+ Feed.P = 101325;
+ Recycle.compMolFrac[1, :] = {0.94629488, 0.053705118};
+ Recycle.T = 348.524;
+ Recycle.totMolFlo[1] = 155.043;
+ Recycle.P = 101325;
+ LPC.condensor.P = 101325;
+ LPC.reboiler.P = 101325;
+ HPC.condensor.P = 1114275;
+ HPC.reboiler.P = 1114275;
+ Distillate1.compMolFrac[1, 1] = 0.99562918;
+ Distillate2.compMolFrac[1, 1] = 0.94629488;
+ Bottoms1.compMolFrac[1, 1] = 0.84105323;
+ Bottoms2.compMolFrac[1, 2] = 0.995;
+ cooler1.outT = 348;
+ end flowsheet;
+
+ //===============================================================================================
+
+ package LPC
+ model Condensor
+ extends Simulator.Unit_Operations.Distillation_Column.Cond;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+ end Condensor;
+
+ model Tray
+ extends Simulator.Unit_Operations.Distillation_Column.DistTray;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+ end Tray;
+
+ model Reboiler
+ extends Simulator.Unit_Operations.Distillation_Column.Reb;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+ end Reboiler;
+
+ model DistColumn
+ extends Simulator.Unit_Operations.Distillation_Column.DistCol;
+ Condensor condensor(NOC = NOC, comp = comp, condType = condType, boolFeed = boolFeed[1], T(start = 300));
+ Reboiler reboiler(NOC = NOC, comp = comp, boolFeed = boolFeed[noOfStages]);
+ Tray tray[noOfStages - 2](each NOC = NOC, each comp = comp, boolFeed = boolFeed[2:noOfStages - 1], each liqMolFlo(each start = 150), each vapMolFlo(each start = 150));
+ end DistColumn;
+ end LPC;
+
+ package HPC
+ model Condensor
+ extends Simulator.Unit_Operations.Distillation_Column.Cond;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+ end Condensor;
+
+ model Tray
+ extends Simulator.Unit_Operations.Distillation_Column.DistTray;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+ end Tray;
+
+ model Reboiler
+ extends Simulator.Unit_Operations.Distillation_Column.Reb;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+ end Reboiler;
+
+ model DistColumn
+ extends Simulator.Unit_Operations.Distillation_Column.DistCol;
+ Condensor condensor(NOC = NOC, comp = comp, condType = condType, boolFeed = boolFeed[1], T(start = 300));
+ Reboiler reboiler(NOC = NOC, comp = comp, boolFeed = boolFeed[noOfStages]);
+ Tray tray[noOfStages - 2](each NOC = NOC, each comp = comp, boolFeed = boolFeed[2:noOfStages - 1], each liqMolFlo(each start = 150), each vapMolFlo(each start = 150));
+ end DistColumn;
+ end HPC;
+end Pres_swin_Dist;
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
new file mode 100644
index 0000000..28315d1
--- /dev/null
+++ b/Pressure_Swing_Distillation_Of_Ethanol-Water_Mixture_By_Mr_Kaushik_Datta/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Pressure Swing Distillation of Ethanol-Water Mixture
+Proposar Name: Mr Kaushik Datta
+University: Indian Institute of Technology Bombay
+
+
+OpenModelica Flowsheet Project By FOSSEE, IIT Bombay
generated by cgit (git 2.34.1) at 2024-12-22 09:47:44 +0000