Thermo and Aspen Terry A. Ring.

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Presentation transcript:

Thermo and Aspen Terry A. Ring

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.

Aspen Process Simulation Software Does All Mass Balances Mole balances for reactions Does All Energy Balances Keeps Track of Thermo Phase Equilibrium Reaction Equilibrium

Thermo Methods

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.