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| author | Sashi20 | 2020-01-10 15:45:15 +0530 |
|---|---|---|
| committer | Sashi20 | 2020-01-10 15:45:15 +0530 |
| commit | 20287f1d05e348d7e7cd4e8d4336a0d70e7f5016 (patch) | |
| tree | 9c65be7121e3151ec81cd4f6838e121cdb97bb4a /Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta | |
| download | OM-Flowsheets-20287f1d05e348d7e7cd4e8d4336a0d70e7f5016.tar.gz OM-Flowsheets-20287f1d05e348d7e7cd4e8d4336a0d70e7f5016.tar.bz2 OM-Flowsheets-20287f1d05e348d7e7cd4e8d4336a0d70e7f5016.zip | |
first commit
Diffstat (limited to 'Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta')
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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 Binary files differnew file mode 100644 index 0000000..431556e --- /dev/null +++ b/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Abstract.pdf 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 new file mode 100644 index 0000000..caa384f --- /dev/null +++ b/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/Methanol_Water_Sep.mo @@ -0,0 +1,163 @@ +package Methanol_Water_Sep
+
+model ms
+ extends Simulator.Streams.Material_Stream;
+ extends Simulator.Files.Thermodynamic_Packages.Raoults_Law;
+end ms;
+
+
+
+
+package DC_Single
+ 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 DC_Single;
+
+model Main_Flowsheet
+ parameter Integer NOC = 2;
+ import data = Simulator.Files.Chemsep_Database;
+
+ parameter data.Methanol meth;
+ parameter data.Water wat;
+
+ parameter Simulator.Files.Chemsep_Database.General_Properties comp[NOC] = {meth,wat};
+
+ Methanol_Water_Sep.ms Feed(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {-170, 12}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Simulator.Unit_Operations.Splitter Splitter(NOC = NOC, comp = comp, NO = 2, calcType = "Molar_Flow") annotation(
+ Placement(visible = true, transformation(origin = {-122, 12}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ ms Feed_I(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {-70, 32}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ ms Feed_II(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {-72, -28}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Methanol_Water_Sep.DC_Single.DistColumn DC_I(NOC = NOC, comp = comp, noOfStages = 20, feedStages = {10},each tray.liqMolFlo(each start = 700), each tray.vapMolFlo(each start = 800)) annotation(
+ Placement(visible = true, transformation(origin = {15, 33}, extent = {{-23, -23}, {23, 23}}, rotation = 0)));
+ Methanol_Water_Sep.ms Distillate_I(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {74, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Methanol_Water_Sep.ms Bottoms_I(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {76, 6}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ Methanol_Water_Sep.DC_Single.DistColumn DC_II(NOC = NOC, comp = comp, noOfStages = 32, feedStages = {18},each tray.liqMolFlo(each start = 600), each tray.vapMolFlo(each start = 800),each tray.T(each start = 400)) annotation(
+ Placement(visible = true, transformation(origin = {17, -35}, extent = {{-23, -23}, {23, 23}}, rotation = 0)));
+ ms Distillate_II(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {76, -18}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ ms Bottoms_II(NOC=NOC, comp=comp) annotation(
+ Placement(visible = true, transformation(origin = {76, -74}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));
+ equation
+ connect(DC_II.bottoms, Bottoms_II.inlet) annotation(
+ Line(points = {{40, -52}, {48, -52}, {48, -74}, {66, -74}, {66, -74}}));
+ connect(DC_II.distillate, Distillate_II.inlet) annotation(
+ Line(points = {{40, -18}, {66, -18}, {66, -18}, {66, -18}}));
+ connect(Feed_II.outlet, DC_II.feed[1]) annotation(
+ Line(points = {{-62, -28}, {-6, -28}, {-6, -36}, {-6, -36}}));
+ connect(DC_I.bottoms, Bottoms_I.inlet) annotation(
+ Line(points = {{38, 16}, {42, 16}, {42, 6}, {66, 6}, {66, 6}}));
+ connect(DC_I.distillate, Distillate_I.inlet) annotation(
+ Line(points = {{38, 50}, {48, 50}, {48, 68}, {64, 68}, {64, 68}}));
+ connect(Feed_I.outlet, DC_I.feed[1]) annotation(
+ Line(points = {{-60, 32}, {-6, 32}, {-6, 32}, {-8, 32}}));
+ connect(Feed.outlet, Splitter.inlet) annotation(
+ Line(points = {{-160, 12}, {-132, 12}}));
+ connect(Feed_I.inlet, Splitter.outlet[1]) annotation(
+ Line(points = {{-80, 32}, {-112, 32}, {-112, 12}}));
+ connect(Feed_II.inlet, Splitter.outlet[2]) annotation(
+ Line(points = {{-82, -28}, {-112, -28}, {-112, 12}}));
+
+ Feed.T = 298.15;
+ Feed.P = 101325;
+ Feed.totMolFlo[1] = 1000;
+ Feed.compMolFrac[1, :] = {0.6,0.4};
+
+ Splitter.specVal = {508.6, 491.4};
+
+ DC_I.condensor.P = 60795;
+ DC_I.reboiler.P = 60795;
+ DC_I.refluxRatio = 2;
+ Distillate_I.totMolFlo[1] = 307.194;
+
+ DC_II.condensor.P = 506625;
+ DC_II.reboiler.P = 506625;
+ DC_II.refluxRatio = 2;
+ Bottoms_II.totMolFlo[1] = 192.716;
+ end Main_Flowsheet;
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+end Methanol_Water_Sep;
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 new file mode 100644 index 0000000..59fe2e7 --- /dev/null +++ b/Methanol-Water_Separation_Using_Neat_Operation_By_Mr_Kaushik_Datta/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Methanol-Water Separation using Neat Operation +Proposar Name: Mr Kaushik Datta +University: Indian Institute of Technology Bombay + + +OpenModelica Flowsheet Project By FOSSEE, IIT Bombay |