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Received June 17, 2009
Accepted July 16, 2009
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Kinetic parameter estimation of the Fischer-Tropsch synthesis reaction on K/Fe-Cu-Al catalysts

1Division of Energy Systems Research, Ajou University, Suwon 443-749, Korea 2Department of Chemical Engineering, Ajou University, Suwon 443-749, Korea 3Korea Research Institute of Chemical Technology, Daejeon 305-600, Korea
mjpark@ajou.ac.kr
Korean Journal of Chemical Engineering, November 2009, 26(6), 1591-1600(10), 10.1007/s11814-009-0341-1
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Abstract

This paper addresses the development of a mathematical model for a fixed-bed reactor where the Fischer-Tropsch synthesis reaction takes place. The model includes the consumption rate of carbon monoxide and the production rates for paraffin and olefin chains (up to the length of 47). The kinetic parameters are estimated using the experimental data under various experimental conditions with the effect of temperature, space velocity, the composition of feed mixture and pressure included. The simulation results with the estimated parameters predict the CO conversion, methane selectivity, paraffin selectivity and the entire distribution of hydrocarbon products satisfactorily. A further investigation on the effect of operating conditions shows that the ratio of hydrogen to carbon monoxide and the pressure are the effective variables for the determination of the entire distribution.

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