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Title: Bimetallic catalysts. V. Kinetics of the hydrogenolysis of butane over Pt-Mo/SiO[sub 2] catalysts

Journal Article · · Journal of Catalysis; (United States)
; ;  [1]
  1. Universite des Sciences et Technologies de Lille, Cedex (France)

The kinetics of the hydrogenolysis of butane on various Pt-Mo catalysts deposited on silica with the same metal content but with various Mo/(Mo + Pt) ratios has been studied. The hydrogenolysis of the two different kinds of C-C bonds has been distinguished. It is shown that the addition of Mo to Pt drastically changes the selectivity of the reaction, but that this selectivity is approximately the same for all the bimetallic Pt-Mo catalysts. Using a rate equation that had already been used for the hydrogenolysis of alkanes (Maurel, R., Leclercq, G., and Leclercq, L., J. Catal. 44, 68 (1975)), calculation has been made of the values of the equilibrium adsorption constants ([lambda]) and those of the rate constants of the C-C bond splitting steps (k) for the hydrogenolysis of the terminal C-C bonds ([lambda][sub 1] and k[sub 1]) and of the middle C-C bond ([lambda][sub 2] and k[sub 2]). In this way it has been shown that only Pt alone, two different intermediaries with high [lambda] values are formed in which the C-C bonds will be broken further with different selectivities but with low rate constants. On the contrary, on all Pt-Mo catalysts, butane is adsorbed as a single intermediate adsorbed species with a much lower adsorption equilibrium constant than on Pt alone, but this adsorbed species is much more reactive (k[sub 1] and k[sub 2]). The adsorption equilibrium constants are the same for all Pt-Mo taking into account the margin of error, which shows that, on all Pt-Mo, butane is adsorbed on the same mixed Pt-Mo site of constant composition whatever the catalyst's composition. The number of these active sites (proportional to k[sub 1] and k[sub 2]) increases as Mo/(Mo + Pt) increases up to 25-30%, then it decreases. 38 refs., 3 figs., 5 tabs.

OSTI ID:
5078463
Journal Information:
Journal of Catalysis; (United States), Vol. 144:1; ISSN 0021-9517
Country of Publication:
United States
Language:
English