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Kinetics and mechanism of carbon monoxide methanation over silica-supported nickel catalysts

Journal Article · · J. Catal.; (United States)
The rate, r, of CO hydrogenation into methane over Ni/SiO/sub 2/ catalysts is shown to vary in a complex way with temperature and pressure. The true activation energy, E/sub 0/, calculated from the Temkin relation (apparent activation energy against the order to CO and extrapolation to zero order), corresponds to that of the hydrogenation of carbon deposited on the surface from the CO dissociation reaction. It is deduced that the active intermediate is the surface carbon, and the rate-determining step the hydrogenation of this intermediate. Kinetic data are qualitatively accounted for assuming the following equation r = ke/sup -E/sub 0//RT/P/sub H/sub 2//(1 - theta/sub CO/)/sup W/ theta/sub CO/ is the surface coverage in nondissociated inactive adsorbed CO molecules which are considered as the most abundant species present on the surface. The parameter W is probably very large (W = 13 on the basis of data of CO + H/sub 2/ over NI-Cu/SiO/sub 2/). In this equation, the term (1 - theta/sub CO/)/sup W/ represents the probability of having W adjacent Ni atoms free from inactive adsorbed CO. This ensemble should be considered as the active site and is covered with one active monocarbon adspecies. 28 references, 6 figures, 1 table.
Research Organization:
Institut de Recherches sur la Catalyse, CNRS, Villeurbanne, France
OSTI ID:
5403739
Journal Information:
J. Catal.; (United States), Journal Name: J. Catal.; (United States) Vol. 84:1; ISSN JCTLA
Country of Publication:
United States
Language:
English

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