The rate of Fischer-Tropsch synthesis over an industrial well-characterized Co-Ru/gamma-Al2O3 catalyst was studied in a laboratory well mixed. continuous flow, slurry reactor under the conditions relevant to industrial operations as follows: temperature of 200-240 degrees C, pressure of 20-35 bar, H-2/CO feed ratio of 1.0-2.5, gas hourly space velocity of 500-1500 N cm(3) g(car)(-1), h(-1) and conversions of 10-84% of carbon monoxide and 13-89% of hydrogen. The ranges of partial pressures of CO and H-2 have been chosen as 5-15 and 10-25 bar respectively. Five kinetic models are considered: one empirical power law model and four variations of the Langmuir-Hinshelwood-Hougen-Watson representation. All models considered incorporate a strong inhibition due to CO adsorption. The data of this study are fitted fairly well by a simple LHHW form -R-H2 (+) (CO) =ap(H2)(0.988)p(CO)(0.508) / (1 + bp(CO)(0.508))(2) in comparison to fits of the same data by several other representative LHHW rate forms proposed in other works. The apparent activation energy was 94-103 kJ/mol. Kinetic parameters are determined using the genetic algorithm approach (CA), followed by the Levenberg-Marquardt (LM) method to make refined optimization, and are validated by means of statistical analysis. Also. the performance of the catalyst for Fischer-Tropsch synthesis and the hydrocarbon product distributions were investigated under different reaction conditions. (C) 2009 Elsevier B.V. All rights reserved.