6 l1-pro max tutorial
TRANSCRIPT
![Page 1: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/1.jpg)
ProMax Tutorial
Terry A. Ring
CH EN 4253
![Page 2: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/2.jpg)
Process Simulation Software
• Steady State Process Simulation– AspenPlus– ProMax– ChemCad– Hysis– HySim– ProSim– CADSim– OLI Process Simulator– KemSimp– Chemical Workbench Code– Ascend IV
• Dynamic Process Simulation– Aspen Dynamics– CADSim – Simulation Solutions, Inc.
![Page 3: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/3.jpg)
OverviewDifferences to Aspen
• Aspen– Next Button
– Many units that perform a given function
• Degrees of Freedom are chosen for you
– Setup for kinetic reactions are tricky
– Accounts for particle sizes• Simple block models
– Automatic Plant Costing (Icarus)
• ProMax– More Thermo Package Choices– Fewer units that perform a given
function• You choose the Degrees of
Freedom– Reaction setup is more straight
forward– Detailed design of
• HX– Reboilers– Condensers
• Distillation Columns– Does not deal with particle sizes– No Plant Costing– Some minor bugs not worked out
![Page 4: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/4.jpg)
Steps to Run
• Aspen (Left Hand Bar)– Title– Components– Thermopackage– Process Flow Sheet– Feed Stream– Unit Specifications
• Fixed degrees of freedom
– Run– Results– Report
• ProMax– Environment
• Components
• Thermopackage
– Process Flow Sheet– Feed Stream– Unit Specifications
• Various degrees of freedom
– Run– Results– Report
![Page 5: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/5.jpg)
Degrees of Freedom
• Statistical Mechanics –Gasses– Gives Heat Capacity of Gasses = NR/2
Monatomic Linear molecules Non-Linear molecules
Position (x, y and z) 3 3 3 Rotation (x, y and z) 0 2 3 Vibration 0 3N - 5 3N - 6 Total 3 3N 3N
![Page 6: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/6.jpg)
Degrees of Freedom
• Phase Diagram– F = C-P+2
• C=Components• P=Phases• 2 = T and P
• Process Simulation• ND= Nvariables-Nequations
• Nvariables for each stream– Mole fractions– Mole flow rate– Enthalpy (T,P)
• Nequations
– Overall Component mole balance
– Mole fractions add to 1.0 for each stream
– Enthalpy Balance
![Page 7: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/7.jpg)
Example-I
• Problem 5.12
• Alternatives in preparing a feed. A process under design requires that 100 lbmol/hr of toluene at 70F and 20 psia be brought to 450 F and 75 psia.
• Flow sheets using Peng-Robinson– Boil-Superheat-Compress– Pump to 75 psi-Boil-Superheat
![Page 8: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/8.jpg)
Problem -2
• Use Gibbs Minimization reactor in Aspen to determine the products of reaction at 10 atm and 200 C.
• Feed equimolar in CO and H2
)(
2
22
32
sCOHHCO
OHCHHCO
![Page 9: 6 l1-pro max tutorial](https://reader035.vdocuments.site/reader035/viewer/2022062319/55869a03d8b42aab558b45fc/html5/thumbnails/9.jpg)
Example-4
• Distillation/Flash
• Isopropanol – Water– 100 lbmole/hr
• Flash at 90C• Distillation
– R=2– BUR=3