ABSTRACT In this paper the effect of changing different supports, calcination temperature and Ni loading on carbon dioxide reforming of methane using Ni-based catalyst are explored experimentally. The supports used are alumina (with different surface areas), silica, titania and zirconia . Calcination temperature is ranged from 773 to 1073 K, while nickel loading is ranged from 0 to 22% .The results showed that calcination at 873 K led to an acceptable catalyst activity. High surface area alumina proved to be the best support in terms of both activity and stability. 12% nickel loading proved to be satisfactory.
H., F., A., S., & A., A. (2006). EFFECT OF CATALYST PREPARATION ON DRY REFORMING OF METHANE. The International Conference on Chemical and Environmental Engineering, 3(3rd International Conference On Chemical & Environmental Engineering), 127-139. doi: 10.21608/iccee.2006.41061
MLA
Fakeeha A. H.; Soliman M. A.; Al-Fatish A. A.. "EFFECT OF CATALYST PREPARATION ON DRY REFORMING OF METHANE". The International Conference on Chemical and Environmental Engineering, 3, 3rd International Conference On Chemical & Environmental Engineering, 2006, 127-139. doi: 10.21608/iccee.2006.41061
HARVARD
H., F., A., S., A., A. (2006). 'EFFECT OF CATALYST PREPARATION ON DRY REFORMING OF METHANE', The International Conference on Chemical and Environmental Engineering, 3(3rd International Conference On Chemical & Environmental Engineering), pp. 127-139. doi: 10.21608/iccee.2006.41061
VANCOUVER
H., F., A., S., A., A. EFFECT OF CATALYST PREPARATION ON DRY REFORMING OF METHANE. The International Conference on Chemical and Environmental Engineering, 2006; 3(3rd International Conference On Chemical & Environmental Engineering): 127-139. doi: 10.21608/iccee.2006.41061
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