The present study reports the synthesis of paraffinic hydrocarbons in the C
-10-C-20 range using a Co/Zr Fischer-Tropsch (FT) eggshell catalyst support
ed on silica. Operating conditions selected for the experimental studies, i
n a Berty-type reactor, are representative of industrial operation. Five ki
netic models are considered: one empirical model and four variations of a L
angmuir-Hinselwood representation. All models considered incorporate a stro
ng inhibition due to CO adsorption. Kinetic parameters are determined using
non-linear regression and are validated by means of statistical analysis.
(C) 2001 Elsevier Science Ltd. All rights reserved.