Some aspects of rate-based modelling and simulation of three-phase distillation columns

Author:

Eckert Egon,Vanĕk Tomáš

Publisher

Elsevier BV

Subject

Computer Science Applications,General Chemical Engineering

Reference20 articles.

1. AIChE, 1958. Bubble Tray Design Manual. New York: AIChE.

2. Measurement and representation of ternary vapour–liquid–liquid equilibria;Connemann;Fluid Phase Equilibrium,1990

3. Düx, A. (1996). Verification of an equilibrium model in dynamic simulation of three–phase distillation. Diploma project. RWTH Aachen (in German).

4. A nonequilibrium model of distillation stage with possible occurrence of two liquid phases;Eckert;Collec. Czech. Chem. Commun.,1995

5. Eckert, E., and Vanĕk, T. (1999a). Simplified rate-based modelling and simulation of three-phase distillation columns. Proceedings of the 18th IASTED Int. Conference MIC'99, Anaheim: ACTA Press, pp. 223–226.

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