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-rw-r--r--Claude_Cycle_For_Nitrogen_Liquefaction_By_Mr_Sarvesh_Sandip_Gaikwad/README.txt8
-rw-r--r--Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Abstract.pdfbin0 -> 442091 bytes
-rw-r--r--Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Flowsheet.dwxmzbin0 -> 110163 bytes
-rw-r--r--Hydrogen_Production_By_Steam_Reforming_Of_Glycerol_By_Mr_Santosh_M_Zol/README.txt8
-rw-r--r--Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet.dwxmzbin0 -> 77676 bytes
-rw-r--r--Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet_Abstract.pdfbin0 -> 140516 bytes
-rw-r--r--Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdfbin0 -> 194181 bytes
-rw-r--r--Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmzbin0 -> 102116 bytes
-rw-r--r--Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Abstract.pdfbin219181 -> 252942 bytes
-rw-r--r--Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Flowsheet.dwxmzbin324139 -> 514669 bytes
-rw-r--r--Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdfbin370155 -> 380523 bytes
-rw-r--r--Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml210
-rw-r--r--Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Abstract.pdfbin0 -> 169697 bytes
-rw-r--r--Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Flowsheet.dwxmzbin0 -> 465720 bytes
14 files changed, 151 insertions, 75 deletions
diff --git a/Claude_Cycle_For_Nitrogen_Liquefaction_By_Mr_Sarvesh_Sandip_Gaikwad/README.txt b/Claude_Cycle_For_Nitrogen_Liquefaction_By_Mr_Sarvesh_Sandip_Gaikwad/README.txt
new file mode 100644
index 0000000..82ec9d6
--- /dev/null
+++ b/Claude_Cycle_For_Nitrogen_Liquefaction_By_Mr_Sarvesh_Sandip_Gaikwad/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Claude Cycle for Nitrogen Liquefaction
+Proposar Name: Mr Sarvesh Sandip Gaikwad
+University: Indian Institue of Technology Madras
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Abstract.pdf b/Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Abstract.pdf
new file mode 100644
index 0000000..97cc624
--- /dev/null
+++ b/Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Abstract.pdf
Binary files differ
diff --git a/Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Flowsheet.dwxmz b/Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Flowsheet.dwxmz
new file mode 100644
index 0000000..ce12826
--- /dev/null
+++ b/Design_And_Control_Of_Acetonitrile_N_-Propanol_Separation_System_Via_Extractive_Distillation_Using_Dimethyl_Sulfoxide_As_Entrainer_By_Mr_Navin_Kumar/Flowsheet.dwxmz
Binary files differ
diff --git a/Hydrogen_Production_By_Steam_Reforming_Of_Glycerol_By_Mr_Santosh_M_Zol/README.txt b/Hydrogen_Production_By_Steam_Reforming_Of_Glycerol_By_Mr_Santosh_M_Zol/README.txt
new file mode 100644
index 0000000..30c3eb3
--- /dev/null
+++ b/Hydrogen_Production_By_Steam_Reforming_Of_Glycerol_By_Mr_Santosh_M_Zol/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Hydrogen Production by Steam Reforming of Glycerol
+Proposar Name: Mr Santosh M Zol
+University: Institute of Chemical Technology Mumbai (Jalna Campus)
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
diff --git a/Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet.dwxmz b/Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet.dwxmz
new file mode 100644
index 0000000..ec22778
--- /dev/null
+++ b/Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet.dwxmz
Binary files differ
diff --git a/Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet_Abstract.pdf b/Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet_Abstract.pdf
new file mode 100644
index 0000000..5e7c74d
--- /dev/null
+++ b/Libr-H2o_Single_Effect_Vapor_Absorption_Refrigeration_Cycle_By_Mr_Emmanuel_M._Saimon/ES_Flowsheet_Abstract.pdf
Binary files differ
diff --git a/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf
new file mode 100644
index 0000000..32a518d
--- /dev/null
+++ b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf
Binary files differ
diff --git a/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz
new file mode 100644
index 0000000..54c3c86
--- /dev/null
+++ b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz
Binary files differ
diff --git a/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Abstract.pdf b/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Abstract.pdf
index 9b80909..4080ea9 100644
--- a/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Abstract.pdf
+++ b/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Abstract.pdf
Binary files differ
diff --git a/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Flowsheet.dwxmz b/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Flowsheet.dwxmz
index ad54854..972dcec 100644
--- a/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Flowsheet.dwxmz
+++ b/Production_Of_Trichloroacetaldehyde_From_Ethanol_By_Mr_Ritik_Odpalliwar_/Flowsheet.dwxmz
Binary files differ
diff --git a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf
index 1b64801..1b2f24d 100644
--- a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf
+++ b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Abstract.pdf
Binary files differ
diff --git a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
index 515f564..575be9f 100644
--- a/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
+++ b/Separation_Of_Acetone_And_Water_Using_Solvent_3-Methylhexane_By_Mr_Pratik_Rathod/Flowsheet.dwxml
@@ -4,7 +4,7 @@
<BuildVersion>8.6.5.0</BuildVersion>
<BuildDate>2000-01-06T00:00:00</BuildDate>
<OSInfo>Microsoft Windows 11 Home Single Language, Version 10.0.22621.0, Win32NT Platform</OSInfo>
- <SavedOn>2023-11-13T20:39:22.014771+05:30</SavedOn>
+ <SavedOn>2024-01-22T14:41:52.8927642+05:30</SavedOn>
<SavedFromClassicUI>true</SavedFromClassicUI>
</GeneralInfo>
<SimulationObjects>
@@ -8396,7 +8396,7 @@
</FlashSettings>
</SelectedPropertyPackage>
<SimulationMode></SimulationMode>
- <BackupFileName>86822447.dwbcs</BackupFileName>
+ <BackupFileName>52647203.dwbcs</BackupFileName>
<FilePath>C:\Users\prati\OneDrive\Documents\Flowsheet.dwxml</FilePath>
<FlowsheetQuickConnect>false</FlowsheetQuickConnect>
<FlowsheetShowCalculationQueue>false</FlowsheetShowCalculationQueue>
@@ -8996,8 +8996,8 @@
<Name>MAT-5da372cf-beda-4763-98f1-cd86c5e18f47</Name>
<Tag>Make-up</Tag>
<Width>20</Width>
- <X>316.5341</X>
- <Y>171.1067</Y>
+ <X>640.4414</X>
+ <Y>256.959</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9043,8 +9043,8 @@
<Name>MAT-db971471-1e8a-42d3-ad06-be461cacea57</Name>
<Tag>Solvent Recovery</Tag>
<Width>20</Width>
- <X>291.0338</X>
- <Y>100.0568</Y>
+ <X>614.9404</X>
+ <Y>185.909</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9090,8 +9090,8 @@
<Name>MAT-9f510731-7729-4083-8c48-1c157b4ee026</Name>
<Tag>Feed</Tag>
<Width>20</Width>
- <X>377.7682</X>
- <Y>43.2431</Y>
+ <X>701.6755</X>
+ <Y>129.0954</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9137,8 +9137,8 @@
<Name>MIST-ae80e666-b984-4270-b427-05f406124fe0</Name>
<Tag>MIX-1</Tag>
<Width>20</Width>
- <X>370.8485</X>
- <Y>145.0467</Y>
+ <X>694.7557</X>
+ <Y>230.8991</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9189,8 +9189,8 @@
<Name>MAT-d392d3ff-4a01-47c1-b8cd-45262f2172dd</Name>
<Tag>S-01</Tag>
<Width>20</Width>
- <X>420.3714</X>
- <Y>155.4365</Y>
+ <X>744.2786</X>
+ <Y>241.2887</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9237,8 +9237,8 @@
<Name>COUO-45389e0d-86e2-4adc-bdcc-54b7f8d38694</Name>
<Tag>EDC-01</Tag>
<Width>144</Width>
- <X>477.2569</X>
- <Y>25.74233</Y>
+ <X>801.1638</X>
+ <Y>111.5946</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9286,8 +9286,8 @@
<Name>MAT-03b2c90d-8474-4909-bef0-39eb7b0a6f41</Name>
<Tag>S-02</Tag>
<Width>20</Width>
- <X>653.9861</X>
- <Y>42.16959</Y>
+ <X>977.8931</X>
+ <Y>128.0219</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9333,8 +9333,8 @@
<Name>MAT-8ab81e9e-3fe4-4e3e-826a-a4926c947b0b</Name>
<Tag>Water</Tag>
<Width>20</Width>
- <X>638.2234</X>
- <Y>224.5327</Y>
+ <X>962.1305</X>
+ <Y>310.3851</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9381,8 +9381,8 @@
<Name>COUO-1ea327c9-e43b-4061-8522-62cdfff084b8</Name>
<Tag>DC-01</Tag>
<Width>144</Width>
- <X>720.1278</X>
- <Y>42.01218</Y>
+ <X>1044.035</X>
+ <Y>127.8646</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9429,8 +9429,8 @@
<Name>MAT-8945f5e3-1173-41b4-b25e-51fbfe116943</Name>
<Tag>Acetone</Tag>
<Width>20</Width>
- <X>925.4</X>
- <Y>48.04378</Y>
+ <X>1249.308</X>
+ <Y>133.8961</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9476,8 +9476,8 @@
<Name>MAT-af8600c0-de0b-4e76-9a4a-33d7f0877225</Name>
<Tag>3-Methylhexane</Tag>
<Width>20</Width>
- <X>891.114</X>
- <Y>228.9925</Y>
+ <X>1215.021</X>
+ <Y>314.8448</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9523,8 +9523,8 @@
<Name>RESF-26c14620-b257-493a-b6d0-b997b40f8564</Name>
<Tag>CL-01</Tag>
<Width>25</Width>
- <X>742.8982</X>
- <Y>278.1421</Y>
+ <X>1066.806</X>
+ <Y>363.9943</Y>
<Selected>false</Selected>
<Rotation>180</Rotation>
<DrawMode>2</DrawMode>
@@ -9571,8 +9571,8 @@
<Name>EN-2eb2db7b-af40-4a5c-a854-e65a6bf3c9bd</Name>
<Tag>E-01</Tag>
<Width>20</Width>
- <X>764.0726</X>
- <Y>315.2731</Y>
+ <X>1087.98</X>
+ <Y>401.1252</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9618,8 +9618,8 @@
<Name>MAT-7163e870-a957-43da-8cc9-c5c97bbddd42</Name>
<Tag>S-03</Tag>
<Width>20</Width>
- <X>640.9811</X>
- <Y>288.7796</Y>
+ <X>964.8884</X>
+ <Y>374.6318</Y>
<Selected>false</Selected>
<Rotation>181</Rotation>
<DrawMode>2</DrawMode>
@@ -9665,8 +9665,8 @@
<Name>REC-7dbf1e49-f6cb-48da-811b-811ed0e42b1f</Name>
<Tag>R-1</Tag>
<Width>20</Width>
- <X>411.9529</X>
- <Y>261.9022</Y>
+ <X>735.8597</X>
+ <Y>347.7545</Y>
<Selected>false</Selected>
<Rotation>180</Rotation>
<DrawMode>2</DrawMode>
@@ -9684,14 +9684,33 @@
<GraphicObject>
<Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.MasterTableGraphic</Type>
<ClipboardData>Master Property Table
-Object Water Solvent Recovery Make-up Feed Acetone 3-Methylhexane
-Temperature 12.3335 25 25 25 57.7331 95.7602 C
-Pressure 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 bar
-Mass Flow 20.0582 173.272 150 100 215.979 173.272 kg/h
-Molar Flow 1.06482 2.80861 1.49698 2.62831 2.80861 2.80861 kmol/h
-Volumetric Flow 0.0201646 0.215989 0.219095 0.113715 0.304737 0.231667 m3/h
-Molar Enthalpy (Mixture) -973.015 7.79216 14.8297 413.471 7172.99 11464.7 kJ/kmol
-Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[kmol.K]
+Object Water Solvent Recovery S-03 S-02 S-01 Make-up Feed Acetone 3-Methylhexane
+Temperature 12.3335 25 25 61.0551 25.0011 25 25 57.7331 95.7602 C
+Pressure 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 1.01325 bar
+Mass Flow 20.0582 173.272 173.272 389.252 309.31 150 100 215.979 173.272 kg/h
+Molar Flow 1.06482 2.80861 2.80861 5.61721 4.05372 1.49698 2.62831 2.80861 2.80861 kmol/h
+Volumetric Flow 0.0201646 0.215989 0.215989 0.526433 0.410688 0.219095 0.113715 0.304737 0.231667 m3/h
+Density (Vapor) 0 0 0 0 0 0 0 0 0 kg/m3
+Molecular Weight (Vapor) 0 0 0 0 0 0 0 0 0 kg/kmol
+Dynamic Viscosity (Vapor) 0 0 0 0 0 0 0 0 0 Pa.s
+Heat Capacity (Vapor) 0 0 0 0 0 0 0 0 0 kJ/[kg.K]
+Compressibility Factor (Vapor) 0 0 0 0 0 0 0 0 0
+Molar Fraction (Vapor) 0 0 0 0 0 0 0 0 0
+Mass Fraction (Vapor) 0 0 0 0 0 0 0 0 0
+Volumetric Fraction (Vapor) 0 0 0 0 0 0 0 0 0
+Density (Liquid 1) 994.725 802.227 802.227 739.414 753.15 684.636 879.388 708.74 747.936 kg/m3
+Molar Weight (Liquid 1) 18.8371 61.6934 61.6934 69.2963 76.3027 100.202 38.0472 76.8992 61.6934 kg/kmol
+Dynamic Viscosity (Liquid 1) 0.00122402 0.000605165 0.000605165 0.000293164 0.000507337 0.000347326 0.000602427 0.00025203 0.000233766 Pa.s
+Heat Capacity (Liquid 1) 0 0 0 0 0 0 0 0 0 kJ/[kg.K]
+Molar Fraction (Liquid 1) 1 1 1 1 1 1 1 1 1
+Mass Fraction (Liquid 1) 1 1 1 1 1 1 1 1 1
+Volumetric Fraction (Liquid 1) 1 1 1 1 1 1 1 1 1
+Molar Fraction (Vapor) / Acetone 2.12621E-12 1.07349E-12 1.07349E-12 0.731687 6.69034E-13 0 0.897742 0.754535 4.7154E-13
+Molar Fraction (Liquid 1) / Acetone 9.39876E-15 2.19234E-14 2.19234E-14 0.233952 1.77051E-14 0 0.5 0.467904 2.19234E-14
+Molar Fraction (Vapor) / Water 0.97027 0.253471 0.253471 0.0630818 0.136373 0 0.102258 0.0127444 0.402308
+Molar Fraction (Liquid 1) / Water 0.99 0.46855 0.46855 0.256136 0.290792 0 0.5 0.0437225 0.46855
+Molar Fraction (Vapor) / 3-methylhexane 0.0297297 0.746529 0.746529 0.205231 0.863627 1 0 0.232721 0.597692
+Molar Fraction (Liquid 1) / 3-methylhexane 0.01 0.53145 0.53145 0.509912 0.709208 1 0 0.488374 0.53145
</ClipboardData>
<NumberOfLines>1</NumberOfLines>
<Padding>4</Padding>
@@ -9703,6 +9722,9 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<SortedList>
<Item>Water</Item>
<Item>Solvent Recovery</Item>
+ <Item>S-03</Item>
+ <Item>S-02</Item>
+ <Item>S-01</Item>
<Item>Make-up</Item>
<Item>Feed</Item>
<Item>Acetone</Item>
@@ -9715,7 +9737,7 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<GradientMode>true</GradientMode>
<LineColor>#fffa8072</LineColor>
<LineColorDark>#fff5f5f5</LineColorDark>
- <Fill>false</Fill>
+ <Fill>true</Fill>
<FillColor>#ffd3d3d3</FillColor>
<FillColorDark>#ffffffff</FillColorDark>
<GradientColor1>#ffd3d3d3</GradientColor1>
@@ -9734,13 +9756,13 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<ShapeOverride>DefaultShape</ShapeOverride>
<Status>NotCalculated</Status>
<AutoSize>true</AutoSize>
- <Height>162</Height>
+ <Height>504</Height>
<IsConnector>false</IsConnector>
<Name>MASTERTABLE-94b87b53-789f-4e15-9f26-07a3eff3148b</Name>
<Tag></Tag>
- <Width>719</Width>
- <X>250.6318</X>
- <Y>378.0211</Y>
+ <Width>1064</Width>
+ <X>457.6452</X>
+ <Y>471.6777</Y>
<Selected>false</Selected>
<Rotation>0</Rotation>
<DrawMode>2</DrawMode>
@@ -9751,11 +9773,11 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
</EnergyConnector>
<SpecialConnectors />
<Objects>
- <S-03>false</S-03>
+ <S-03>true</S-03>
<_x0033_-Methylhexane>true</_x0033_-Methylhexane>
<Acetone>true</Acetone>
- <S-01>false</S-01>
- <S-02>false</S-02>
+ <S-01>true</S-01>
+ <S-02>true</S-02>
<Water>true</Water>
<Feed>true</Feed>
<Solvent_x0020_Recovery>true</Solvent_x0020_Recovery>
@@ -9771,27 +9793,27 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<PROP_MS_6>false</PROP_MS_6>
<PROP_MS_7>false</PROP_MS_7>
<PROP_MS_8>false</PROP_MS_8>
- <PROP_MS_9>true</PROP_MS_9>
- <PROP_MS_10>true</PROP_MS_10>
+ <PROP_MS_9>false</PROP_MS_9>
+ <PROP_MS_10>false</PROP_MS_10>
<PROP_MS_11>false</PROP_MS_11>
- <PROP_MS_12>false</PROP_MS_12>
- <PROP_MS_13>false</PROP_MS_13>
+ <PROP_MS_12>true</PROP_MS_12>
+ <PROP_MS_13>true</PROP_MS_13>
<PROP_MS_14>false</PROP_MS_14>
<PROP_MS_15>false</PROP_MS_15>
<PROP_MS_16>false</PROP_MS_16>
<PROP_MS_17>false</PROP_MS_17>
<PROP_MS_18>false</PROP_MS_18>
<PROP_MS_19>false</PROP_MS_19>
- <PROP_MS_20>false</PROP_MS_20>
- <PROP_MS_21>false</PROP_MS_21>
+ <PROP_MS_20>true</PROP_MS_20>
+ <PROP_MS_21>true</PROP_MS_21>
<PROP_MS_22>false</PROP_MS_22>
<PROP_MS_23>false</PROP_MS_23>
<PROP_MS_24>false</PROP_MS_24>
<PROP_MS_25>false</PROP_MS_25>
- <PROP_MS_26>false</PROP_MS_26>
- <PROP_MS_27>false</PROP_MS_27>
- <PROP_MS_28>false</PROP_MS_28>
- <PROP_MS_29>false</PROP_MS_29>
+ <PROP_MS_26>true</PROP_MS_26>
+ <PROP_MS_27>true</PROP_MS_27>
+ <PROP_MS_28>true</PROP_MS_28>
+ <PROP_MS_29>true</PROP_MS_29>
<PROP_MS_30>false</PROP_MS_30>
<PROP_MS_31>false</PROP_MS_31>
<PROP_MS_32>false</PROP_MS_32>
@@ -9810,24 +9832,24 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<PROP_MS_45>false</PROP_MS_45>
<PROP_MS_46>false</PROP_MS_46>
<PROP_MS_47>false</PROP_MS_47>
- <PROP_MS_48>false</PROP_MS_48>
- <PROP_MS_49>false</PROP_MS_49>
+ <PROP_MS_48>true</PROP_MS_48>
+ <PROP_MS_49>true</PROP_MS_49>
<PROP_MS_50>false</PROP_MS_50>
<PROP_MS_51>false</PROP_MS_51>
<PROP_MS_52>false</PROP_MS_52>
<PROP_MS_53>false</PROP_MS_53>
<PROP_MS_54>false</PROP_MS_54>
<PROP_MS_55>false</PROP_MS_55>
- <PROP_MS_56>false</PROP_MS_56>
- <PROP_MS_57>false</PROP_MS_57>
+ <PROP_MS_56>true</PROP_MS_56>
+ <PROP_MS_57>true</PROP_MS_57>
<PROP_MS_58>false</PROP_MS_58>
<PROP_MS_59>false</PROP_MS_59>
<PROP_MS_60>false</PROP_MS_60>
<PROP_MS_61>false</PROP_MS_61>
<PROP_MS_62>false</PROP_MS_62>
- <PROP_MS_63>false</PROP_MS_63>
- <PROP_MS_64>false</PROP_MS_64>
- <PROP_MS_65>false</PROP_MS_65>
+ <PROP_MS_63>true</PROP_MS_63>
+ <PROP_MS_64>true</PROP_MS_64>
+ <PROP_MS_65>true</PROP_MS_65>
<PROP_MS_66>false</PROP_MS_66>
<PROP_MS_67>false</PROP_MS_67>
<PROP_MS_68>false</PROP_MS_68>
@@ -9886,9 +9908,9 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<PROP_MS_103_x002F_Acetone>false</PROP_MS_103_x002F_Acetone>
<PROP_MS_104_x002F_Acetone>false</PROP_MS_104_x002F_Acetone>
<PROP_MS_105_x002F_Acetone>false</PROP_MS_105_x002F_Acetone>
- <PROP_MS_106_x002F_Acetone>false</PROP_MS_106_x002F_Acetone>
+ <PROP_MS_106_x002F_Acetone>true</PROP_MS_106_x002F_Acetone>
<PROP_MS_107_x002F_Acetone>false</PROP_MS_107_x002F_Acetone>
- <PROP_MS_108_x002F_Acetone>false</PROP_MS_108_x002F_Acetone>
+ <PROP_MS_108_x002F_Acetone>true</PROP_MS_108_x002F_Acetone>
<PROP_MS_109_x002F_Acetone>false</PROP_MS_109_x002F_Acetone>
<PROP_MS_110_x002F_Acetone>false</PROP_MS_110_x002F_Acetone>
<PROP_MS_111_x002F_Acetone>false</PROP_MS_111_x002F_Acetone>
@@ -9914,9 +9936,9 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<PROP_MS_103_x002F_Water>false</PROP_MS_103_x002F_Water>
<PROP_MS_104_x002F_Water>false</PROP_MS_104_x002F_Water>
<PROP_MS_105_x002F_Water>false</PROP_MS_105_x002F_Water>
- <PROP_MS_106_x002F_Water>false</PROP_MS_106_x002F_Water>
+ <PROP_MS_106_x002F_Water>true</PROP_MS_106_x002F_Water>
<PROP_MS_107_x002F_Water>false</PROP_MS_107_x002F_Water>
- <PROP_MS_108_x002F_Water>false</PROP_MS_108_x002F_Water>
+ <PROP_MS_108_x002F_Water>true</PROP_MS_108_x002F_Water>
<PROP_MS_109_x002F_Water>false</PROP_MS_109_x002F_Water>
<PROP_MS_110_x002F_Water>false</PROP_MS_110_x002F_Water>
<PROP_MS_111_x002F_Water>false</PROP_MS_111_x002F_Water>
@@ -9942,9 +9964,9 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<PROP_MS_103_x002F_3-methylhexane>false</PROP_MS_103_x002F_3-methylhexane>
<PROP_MS_104_x002F_3-methylhexane>false</PROP_MS_104_x002F_3-methylhexane>
<PROP_MS_105_x002F_3-methylhexane>false</PROP_MS_105_x002F_3-methylhexane>
- <PROP_MS_106_x002F_3-methylhexane>false</PROP_MS_106_x002F_3-methylhexane>
+ <PROP_MS_106_x002F_3-methylhexane>true</PROP_MS_106_x002F_3-methylhexane>
<PROP_MS_107_x002F_3-methylhexane>false</PROP_MS_107_x002F_3-methylhexane>
- <PROP_MS_108_x002F_3-methylhexane>false</PROP_MS_108_x002F_3-methylhexane>
+ <PROP_MS_108_x002F_3-methylhexane>true</PROP_MS_108_x002F_3-methylhexane>
<PROP_MS_109_x002F_3-methylhexane>false</PROP_MS_109_x002F_3-methylhexane>
<PROP_MS_110_x002F_3-methylhexane>false</PROP_MS_110_x002F_3-methylhexane>
<PROP_MS_111_x002F_3-methylhexane>false</PROP_MS_111_x002F_3-methylhexane>
@@ -10145,10 +10167,48 @@ Molar Entropy (Mixture) -3.4083 0.026135 0.0497392 1.38679 21.6783 31.0771 kJ/[k
<SortableItem>Molar Flow | DESC</SortableItem>
<SortableItem>Volumetric Flow | ASC</SortableItem>
<SortableItem>Volumetric Flow | DESC</SortableItem>
- <SortableItem>Molar Enthalpy (Mixture) | ASC</SortableItem>
- <SortableItem>Molar Enthalpy (Mixture) | DESC</SortableItem>
- <SortableItem>Molar Entropy (Mixture) | ASC</SortableItem>
- <SortableItem>Molar Entropy (Mixture) | DESC</SortableItem>
+ <SortableItem>Density (Vapor) | ASC</SortableItem>
+ <SortableItem>Density (Vapor) | DESC</SortableItem>
+ <SortableItem>Molecular Weight (Vapor) | ASC</SortableItem>
+ <SortableItem>Molecular Weight (Vapor) | DESC</SortableItem>
+ <SortableItem>Dynamic Viscosity (Vapor) | ASC</SortableItem>
+ <SortableItem>Dynamic Viscosity (Vapor) | DESC</SortableItem>
+ <SortableItem>Heat Capacity (Vapor) | ASC</SortableItem>
+ <SortableItem>Heat Capacity (Vapor) | DESC</SortableItem>
+ <SortableItem>Compressibility Factor (Vapor) | ASC</SortableItem>
+ <SortableItem>Compressibility Factor (Vapor) | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) | DESC</SortableItem>
+ <SortableItem>Mass Fraction (Vapor) | ASC</SortableItem>
+ <SortableItem>Mass Fraction (Vapor) | DESC</SortableItem>
+ <SortableItem>Volumetric Fraction (Vapor) | ASC</SortableItem>
+ <SortableItem>Volumetric Fraction (Vapor) | DESC</SortableItem>
+ <SortableItem>Density (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Density (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Molar Weight (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Molar Weight (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Dynamic Viscosity (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Dynamic Viscosity (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Heat Capacity (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Heat Capacity (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Mass Fraction (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Mass Fraction (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Volumetric Fraction (Liquid 1) | ASC</SortableItem>
+ <SortableItem>Volumetric Fraction (Liquid 1) | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) / Acetone | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) / Acetone | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) / Acetone | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) / Acetone | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) / Water | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) / Water | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) / Water | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) / Water | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) / 3-methylhexane | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Vapor) / 3-methylhexane | DESC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) / 3-methylhexane | ASC</SortableItem>
+ <SortableItem>Molar Fraction (Liquid 1) / 3-methylhexane | DESC</SortableItem>
<SortableItem>Custom</SortableItem>
</SortableItems>
</GraphicObject>
diff --git a/Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Abstract.pdf b/Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Abstract.pdf
new file mode 100644
index 0000000..ad6f2cd
--- /dev/null
+++ b/Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Abstract.pdf
Binary files differ
diff --git a/Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Flowsheet.dwxmz b/Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Flowsheet.dwxmz
new file mode 100644
index 0000000..edf3842
--- /dev/null
+++ b/Simulation_Of_High_Pressure_Separator_Used_In_Crude_Oil_Processing_By_Ms_Priscila_Haro/Flowsheet.dwxmz
Binary files differ
generated by cgit (git 2.34.1) at 2025-01-25 17:07:15 +0000