Mechanochemical activation of catalysts for CO2 methanation
β Scribed by S. Mori; W.-C. Xu; T. Ishidzuki; N. Ogasawara; J. Imai; K. Kobayashi
- Publisher
- Elsevier Science
- Year
- 1996
- Tongue
- English
- Weight
- 716 KB
- Volume
- 137
- Category
- Article
- ISSN
- 0926-860X
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β¦ Synopsis
The hydrogenation of CO 2 to CH 4 was carried out using MgO-mixed catalysts of Ru, Ni, Fe or their combinations at temperatures ranging from 80 to 150Β°C under initial pressures of 100 Tort CO 2 and 500 Torr H 2. The effect of the mechanical milling of catalysts on the reaction was investigated. It was found that (1) the yield of CH 4 strongly depended on the kind of catalysts; the highest yield was achieved with Ru-MgO catalyst and the lowest yield with Ni-Fe catalyst. (2) Mechanochemically activated catalysts largely increased the production rate of CH 4 and considerably decreased the activation energy of the reaction from 74 kJ/mol to 41 kJ/mol for Ru-MgO catalyst.
π SIMILAR VOLUMES
A model related to variation in the concentration of active centers is proposed. Previously obtained experimental results are briefly reviewed together with presentation of complementary results. The results are generalized in the assumptions of the model. Two steps of activation of the Co foil are
Two series of Ni/MgO catalysts were prepared by reducing NiO/MgO samples of fixed Ni loading but different calcination temperatures and of varying Ni loadings but fixed calcination temperature. These catalysts were investigated in CO 2 reforming of methane under atmospheric pressure and characterize