Industrial & Engineering Chemistry Research · 1998 · 48 citations · 7 references
The hydrodesulfurization of 4-methyldibenzothiophene and 4,6-dimethyldibenzothiophene on a commercial CoMo/Al2O3 catalyst was studied in a multiphase flow reactor in the presence of dibenzothiophene. Hougen−Watson rate equations for the hydrogenolysis of 4-methyldibenzothiophene into 3-methylbiphenyl and H2S and for the hydrogenation of 4-methyldibenzothiophene into partially hydrogenated intermediates were developed. In an identical manner Hougen−Watson kinetics were determined for the hydrogenolysis of 4,6-dimethyldibenzothiophene into 3,3‘-dimethylbiphenyl and H2S and for the hydrogenation of 4,6-dimethyldibenzothiophene into dimethyltetra- and dimethylhexahydrodibenzothiophene. Two different types of active sites exist on the catalyst surface: σ sites for hydrogenolysis and τ sites for hydrogenation reactions. The surface reaction between adsorbed reactants and two competitively adsorbed hydrogen atoms was the rate-determining step for both types of reaction.
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Chemical reactor analysis and design
Bryan W. Brooks · The Chemical Engineering Journal · 1991 · 2.2K citations
D KILANOWSKI · Journal of Catalysis · 1978 · 135 citations · Full text