A comparative study of CO and CO{sub 2} hydrogenation over Rh/SiO{sub 2}
- Lawrence Berkeley National Lab., CA (United States)
The hydrogenation of CO and CO{sub 2} over Rh/SiO{sub 2} have been investigated for the purpose of identifying the similarities and differences between these two reaction systems. In situ infrared spectroscopy was used to characterize the surface of the catalyst. Exposure of the catalyst to CO or CO{sub 2} produced very similar infrared spectra in which the principal features are those for linearly and bridge-bonded CO. In the case of CO{sub 2} adsorption, a band for weakly adsorbed CO{sub 2} could also be observed. For identical reaction conditions the rate of CO{sub 2} could also be observed. For identical reaction conditions the rate of CO{sub 2} hydrogenation to methane is higher than that for CO hydrogenation. The activation energy for CO hydrogenation is 23.2 kcal/mol and that for CO{sub 2} hydrogenation is 16.6 kcal/mol. The partial pressure dependances on H{sub 2} and CO{sub z} (z = 1, 2) are 0.67 and -0.80, respectively, for CO hydrogenation, and 0.53 and -0.46, respectively, for CO{sub 2} hydrogenation. Infrared spectroscopy reveals that under reaction conditions the catalyst surface is nearly saturated by absorbed CO. The spectra observed during CO and CO{sub 2} hydrogenation are similar, the principal difference being that the CO coverage during CO hydrogenation is somewhat higher than that during CO{sub 2} hydrogenation. The CO coverage is insensitive to H{sub 2} partial pressure, but increases slightly with increasing CO{sub z} partial pressure. Transient-response experiments demonstrate that the adsorbed CO is a critical intermediate in both reaction systems. It is proposed that the rate determining step in the formation of methane is the dissociation of H{sub 2}CO, produced by the stepwise hydrogenation of adsorbed CO. A rate expression derived from the proposed mechanism properly describes the experimentally observed reaction kinetics both under steady-state and transient-response conditions. 88 refs., 17 figs., 3 tabs.
- DOE Contract Number:
- AC03-76SF00098
- OSTI ID:
- 508441
- Journal Information:
- Journal of Catalysis, Journal Name: Journal of Catalysis Journal Issue: 1 Vol. 162; ISSN JCTLA5; ISSN 0021-9517
- Country of Publication:
- United States
- Language:
- English
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