1977 Volume 1977 Issue 3 Pages 315-319
Effects of K2CO3 on the decomposition of butane, and on the reaction of butane with steam, over supported nickel catalysts at 400-500°C were studied.
Addition of K2CO3 to the catalysts brought about no effect on the degree of butane decomposition. The composition of carbon deposit, CH0.2 on the average, at 460°C, obtained by the reaction over the catalysts containing K2CO3, did not differ from that without K2CO3. On the other hand, in the reaction of butane with steam the activity of the catalysts not containing K2CO3 decreased with time. When K2CO3 was added, the lapsing decay of catalysts was improved, despite the stationary activity decreased.
These experimental results were explained in terms of the reaction mechanism that butane and water were adsorbed on a nickel surface competitively, and then the reaction occurred between these adsorbed species. It was concluded that when water was absent or the amount of water on the surface was not sufficient, the adsorbed butane might decompose to form carbon deposit.
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