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Kinetics of the complex oxidation of methane over supported palladium catalysts

Journal Article · · Journal of Catalysis; (United States)
; ;  [1]
  1. Catalytica Inc., Mountain View, CA (United States)
The complete oxidation of methane by supported Pd was studied in a reaction mixture of 2% CH[sub 4] in air at 550 K, and atmospheric pressure. The catalysts were Pd supported on Al[sub 2]O[sub 3] and ZrO[sub 2] deposited from PdCl[sub 2] or Pd(NH[sub 3])[sub 2](NO[sub 2])[sub 2] precursors. For the determination of how the turnover rate varies with the structure of the catalyst, the average Pd particle size on the series of catalysts was varied in the critical size range (1-10 nm). The number of active sites were measured before and after reaction by the method of H[sub 2] titration of adsorbed oxygen at 373 K. The number of active sites remained the same, although the rate per gram of catalyst increased with time on-stream for all catalysts. At steady-state, the turnover rate for the series of catalysts tested varied in the range 2 [times] 10[sup [minus]2] to 8 [times] 10[sup [minus]2] s[sup [minus]1] under the conditions of these experiments. It is concluded that the reaction is structure insensitive. In an investigation of the kinetics of methane oxidation on palladium, the reaction products were found to strongly inhibit the oxidation of methane. 32 refs., 6 figs., 4 tabs.
OSTI ID:
7036594
Journal Information:
Journal of Catalysis; (United States), Journal Name: Journal of Catalysis; (United States) Vol. 146:2; ISSN 0021-9517; ISSN JCTLA5
Country of Publication:
United States
Language:
English