Abstract
In the reported experimental study, the kinetics of the steam reforming of methane (CH//4 plus H//2O yields CO plus 3H//2) have been examined over a commerical co-precipitated nickel alumina catalyst and over a nickel catalyst supported on gamma -alumina. The mechanism of the reaction is shown to be different over each catalyst, and this conclusion is confirmed by CH//4 plus D//2O experiments. The two mechanisms are discussed. The results for the CH//4 plus D//2O reaction over other impregnated catalysts are also presented. The results for all the catalysts are discussed in terms of the catalyst structure.
Original language | English |
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Pages | 201-214 |
Number of pages | 14 |
Publication status | Published - 1975 |
Event | Mech of Hydrocarbon React, Symp, Proc, Siofok - Duration: 5 Jun 1973 → 7 Jun 1973 |
Conference
Conference | Mech of Hydrocarbon React, Symp, Proc, Siofok |
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Period | 5/06/73 → 7/06/73 |