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

 R  Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./Abstract_DryMethaneReformingProcess.pdf -> Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Abstract_DryMethaneReformingProcess.pdf
R  Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./Flowsheet_DryMethaneReformingProcess.mo -> Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Flowsheet_DryMethaneReformingProcess.mo
R  Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./README.txt -> Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/README.txt
A  Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/Flowsheet_PSDEthyl.mo
A  Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/README.txt
A  Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/abstract.pdf

6 files changed, 155 insertions, 0 deletions

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
index 984c03c..984c03c 100644
--- a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./Abstract_DryMethaneReformingProcess.pdf
+++ b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Abstract_DryMethaneReformingProcess.pdf
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
index 46d51b9..46d51b9 100644
--- a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./Flowsheet_DryMethaneReformingProcess.mo
+++ b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/Flowsheet_DryMethaneReformingProcess.mo
diff --git a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./README.txt b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/README.txt
index 1fbc303..1fbc303 100644
--- a/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S./README.txt
+++ b/Dry_Methane_Reforming_Process_By_Mr_Pranaav_S/README.txt
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
new file mode 100644
index 0000000..611fe07
--- /dev/null
+++ b/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/Flowsheet_PSDEthyl.mo
@@ -0,0 +1,147 @@
+package Pres_swin_Dist

+  model Material_Streams

+    //instantiation of chemsep database

+    import data = Simulator.Files.Chemsep_Database;

+    //instantiation of Nhexane

+    parameter data.Nhexane hex;

+    //instantiation of Ethylacetate

+    parameter data.Ethylacetate ethy;

+    extends Simulator.Streams.Material_Stream(NOC = 2, comp = {hex, ethy}, 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.NRTL;

+    //thermodynamic package NRTL is extended

+  end Material_Streams;

+

+  model flowsheet

+    import data = Simulator.Files.Chemsep_Database;

+    //instantiation of Nhexane

+    parameter data.Nhexane hex;

+    //instantiation of Ethylacetate

+    parameter data.Ethylacetate ethy;

+    //Number of Components

+    parameter Integer NOC = 2;

+    parameter data.General_Properties comp[NOC] = {hex, ethy};

+    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)));

+    Pres_swin_Dist.LPC.DistColumn LPC(NOC = NOC, comp = comp, feedStages = {8, 16}, noOfFeeds = 2, noOfStages = 26) 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 = 25) annotation(

+      Placement(visible = true, transformation(origin = {108, 6}, extent = {{-28, -28}, {28, 28}}, rotation = 0)));

+    Pres_swin_Dist.Material_Streams Distillate2(NOC = NOC, comp = comp) annotation(

+      Placement(visible = true, transformation(origin = {162, 62}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));

+    Pres_swin_Dist.Material_Streams Bottoms2(NOC = NOC, comp = comp) annotation(

+      Placement(visible = true, transformation(origin = {174, -36}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));

+    Simulator.Streams.Energy_Stream C_duty2 annotation(

+      Placement(visible = true, transformation(origin = {106, 68}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));

+    Simulator.Streams.Energy_Stream R_duty2 annotation(

+      Placement(visible = true, transformation(origin = {120, -58}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));

+    Material_Streams material1(NOC = NOC, comp = comp) annotation(

+      Placement(visible = true, transformation(origin = {42, 18}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));

+  Simulator.Unit_Operations.Centrifugal_Pump Pump(comp = {hex, ethy}, NOC = 2, eff = 0.75) annotation(

+      Placement(visible = true, transformation(origin = {46, 58}, extent = {{-10, -10}, {10, 10}}, rotation = 0)));

+  equation

+    connect(Pump.outlet, material1.inlet) annotation(

+      Line(points = {{56, 58}, {68, 58}, {68, 36}, {14, 36}, {14, 18}, {32, 18}, {32, 18}}));

+    connect(Distillate1.outlet, Pump.inlet) annotation(

+      Line(points = {{18, 58}, {36, 58}, {36, 58}, {36, 58}}));

+    connect(HPC.bottoms, Bottoms2.inlet) annotation(

+      Line(points = {{136, -14}, {156, -14}, {156, -36}, {164, -36}, {164, -36}}));

+    connect(HPC.distillate, Distillate2.inlet) annotation(

+      Line(points = {{136, 26}, {144, 26}, {144, 62}, {152, 62}, {152, 62}}));

+    connect(HPC.reboiler_duty, R_duty2.outlet) annotation(

+      Line(points = {{128, -22}, {146, -22}, {146, -58}, {130, -58}, {130, -58}}));

+    connect(C_duty2.outlet, HPC.condensor_duty) annotation(

+      Line(points = {{116, 68}, {126, 68}, {126, 32}, {124, 32}}));

+    connect(material1.outlet, HPC.feed[1]) annotation(

+      Line(points = {{52, 18}, {64, 18}, {64, 4}, {80, 4}, {80, 4}}));

+    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}}));

+    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}}));

+    Feed.compMolFrac[1, :] = {0.61525346, 0.38474654};

+    Feed.T = 298.15;

+    Feed.totMolFlo[1] = 3.195817;

+    Feed.P = 101325;

+    Recycle.compMolFrac[1, :] = {0.56249543, 0.43750457};

+    Recycle.T = 345.32519;

+    Recycle.totMolFlo[1] = 55.438505;

+    Recycle.P = 100000;

+    LPC.condensor.P = 100000;

+    LPC.reboiler.P = 100000;

+    HPC.condensor.P = 600000;

+    HPC.reboiler.P = 600000;

+    Pump.pressInc = 500000;

+    Distillate1.compMolFrac[1, 1] = 0.56853542;

+    Distillate2.compMolFrac[1, 1] = 0.56245693;

+    Bottoms1.compMolFrac[1, 2] = 0.97;

+    Bottoms2.compMolFrac[1, 1] = 0.999;

+  end flowsheet;

+

+  //===============================================================================================

+

+  package LPC

+    model Condensor

+      extends Simulator.Unit_Operations.Distillation_Column.Cond;

+      extends Simulator.Files.Thermodynamic_Packages.NRTL;

+    end Condensor;

+

+    model Tray

+      extends Simulator.Unit_Operations.Distillation_Column.DistTray;

+      extends Simulator.Files.Thermodynamic_Packages.NRTL;

+    end Tray;

+

+    model Reboiler

+      extends Simulator.Unit_Operations.Distillation_Column.Reb;

+      extends Simulator.Files.Thermodynamic_Packages.NRTL;

+    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.NRTL;

+    end Condensor;

+

+    model Tray

+      extends Simulator.Unit_Operations.Distillation_Column.DistTray;

+      extends Simulator.Files.Thermodynamic_Packages.NRTL;

+    end Tray;

+

+    model Reboiler

+      extends Simulator.Unit_Operations.Distillation_Column.Reb;

+      extends Simulator.Files.Thermodynamic_Packages.NRTL;

+    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_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
new file mode 100644
index 0000000..1d6f1b7
--- /dev/null
+++ b/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Pressure Swing Distillation of Ethyl Acetate and N-Hexane
+Proposar Name: Mr Kaushik Datta
+University: Indian Institute of Technology Bombay
+
+
+OpenModelica Flowsheet Project By FOSSEE, IIT Bombay
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
new file mode 100644
index 0000000..2bfb084
--- /dev/null
+++ b/Pressure_Swing_Distillation_Of_Ethyl_Acetate_And_N-Hexane_By_Mr_Kaushik_Datta/abstract.pdf