Abstract
The mathematical model and the method of its numerical analysis for fixed-bed catalytic reactors were developed and were applied to the pilot reactor of isopropyl alcohol (IPA). The experimental results from pilot test runs were used to test and verify the simulation results. The numerical simulation gives the IPA concentration and temperature profiles in the reactor. The production of IPA from a commercialized ethanol rector was examined. The operation conditions of IPA synthesis were established.
Article PDF
Similar content being viewed by others
Avoid common mistakes on your manuscript.
References
Hibernia-Chemie GMBH.: Brit. Patent 1,159,667 (1966).
Hibernia-Chemie GMBH.:Hydrocarbon Process.,46(11), 195(1967).
Pullman Inc.: Fren. Patent1, 560,386 (1967).
KRICT(Korea Research Institute of Chemical Technology): Report No. BSR 85-0073 (1985).
KRICT: Report No. BSR 86-0085 (1986).
KRICT: Report No. BSR 87-0086 (1987).
Morse, P.L. : “Synthetic Ethanol and Isopropanol”, SRI Report No. 53 (1969).
Smith, J.M.: “Chemical Engineering Kinetics”, Int. Stud.Ed. (1970).
Carberry, J.J.: “Chemical and Catalytic Reaction Engineering”, McGraw-Hill (1976).
McHenry, K.W. and Wilhelm, R.H.:AfChE J.,3, 83 (1957).
Schwartz, C.E. and Smith, J.M.:I & EC,45, 1209 (1953).
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Kim, DK., Lee, SB. & Yoon, P. Numerical simulation of fixed-bed catalytic reactor for isopropyl alcohol synthesis. Korean J. Chem. Eng. 6, 99–104 (1989). https://doi.org/10.1007/BF02697486
Received:
Accepted:
Issue Date:
DOI: https://doi.org/10.1007/BF02697486