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Introduction to Aspen. Terry A. Ring. 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.
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Introduction to Aspen Terry A. Ring
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. Process Simulation Software
Aspen • Process Simulation Software • Does All Mass Balances • Mole balances for reactions • Does All Energy Balances • Keeps Track of Thermo • Phase Equilibrium • Reaction Equilibrium
Which Thermo Package Do I use? • See Property Prediction PowerPoint
Problem 1 • Vapor Liquid Equilibria • Ethanol – water
Problem 2 • Liquid-Liquid Equilibria • Polar - polar
Problem 3 • Liquid-Liquid Equilibria • Polar - non-polar
Lecture 1- Problem 4 • Multiple component phase equilibria • Methane – 0.1 mole fraction • Ethane – 0.2 • Propane- 0.3 • Butane- 0.3 • Methyl ethyl keytone -0.1 • 10 atm, 10°C • Use Ideal and Peng Robinson Thermo Pkg. • Compare results
Problem -5 • Use Gibbs Minimization reactor in Aspen to determine the products of reaction at 10 atm and 200 C.