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Kinetics and mechanism of ethane hydrogenolysis on silica-supported platinum and platinum-iron catalysts

Journal Article · · J. Catal.; (United States)
A kinetic analysis of ethane hydrogenolysis has been carried out on Pt/SiO/sub 2/ and PtFe/SiO/sub 2/ catalysts with a wide range of concentration of the components, and with an excess of ethane. With the help of the theory of stationary reactions on heterogeneous surfaces, kinetic equations were obtained describing the reaction rate both in excess hydrogen and excess ethane which are in full agreement with the experimental observations. On platinum in excess hydrogen the rate of hydrogenolysis is determined by the C-C bond rupture of ethane adsorbed in a mildly dissociated C/sub 2/H/sub x/ form, while in excess hydrocarbon it is determined by the C-C bond rupture of ethane adsorbed in the deeply dissociated form of C/sub 2/H/sub 2/. The reaction rate passes through a maximum vs ethane pressure at constant hydrogen pressure and vice versa. The formal reaction order in hydrogen and hydrocarbon can be either positive or negative depending on the conditions; the formal power-rate equations may be considered as approximations of the more complicated equations presented in this work. 3 figures, 5 tables.
Research Organization:
Hungarian Academy of Sciences, Budapest
OSTI ID:
5385279
Journal Information:
J. Catal.; (United States), Journal Name: J. Catal.; (United States) Vol. 74:2; ISSN JCTLA
Country of Publication:
United States
Language:
English

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