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MODELING AND SIMULATION OF A SULFOLANE EXTRACTION PROCESS
Korean Journal of Chemical Engineering, January 1998, 15(1), 90-94(5), 10.1007/BF02705311
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Abstract
Modeling and simulation for a sulfolane extraction process were performed. The process investigated in the present work consists of two tray columns, one of which is used for extraction and the other one for washing. The modified θ-method was employed for the modeling of the process. The computation of the equilibrium state of a two-phase system is one of the key issues in the modeling and simulation of extraction processes. In the present work the UNIFAC method was used for the computation of related thermodynamic properties and equilibrium states. Results of simulations showed good agreement with actual plant operation data.
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References
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Boston JF, Shah VB, "An Algorithm for Rigorous Distillation Calculations with Two Liquid Phase," AIChE Meeting, Huston, TX, April (1979)
Brett PC, Ian AF, Ind. Eng. Chem. Res., 29(7), 1364 (1990)
Holland CD, "Fundamentals and Modeling of Separation Processes," Prentice-Hall, New Jersey (1975)
Kovach JW, Seider WD, AIChE J., 33(8), 1300 (1987)
Marcus Y, "Ion Solvation," John Wiley & Sons, Chicester, U.K., 190 (1985)
McKetta JJ, "Benzene from Petroleum," Encyclopedia of Chemical Processing and Design, Dekker, New York (1977)
Panneman HJ, Beenackers AACM, Ind. Eng. Chem. Res., 31(4), 1227 (1992)
Reid CR, Prausnitz JM, Poling BE, "The Properties of Gases and Liquids," 4th ed., McGraw-Hill (1988)
Trevino-Lozano RA, Kisala TP, Boston JF, Comput. Chem. Eng., 8(2), 105 (1984)
Tsuboka T, Katayama T, J. Chem. Eng. Jpn., 9, 40 (1976)
