EFFECT OF CATALYST PREPARATION ON DRY REFORMING OF METHANE | ||||
| The International Conference on Chemical and Environmental Engineering | ||||
| Article 11, Volume 3, 3rd International Conference On Chemical & Environmental Engineering, May 2006, Page 127-139 PDF (373.64 K) | ||||
| Document Type: Original Article | ||||
| DOI: 10.21608/iccee.2006.41061 | ||||
 View on SCiNiTO | ||||
| Authors | ||||
| Fakeeha A. H.; Soliman M. A.; Al-Fatish A. A. | ||||
| College Of Engineering,King Saud University,Saudi Arabia. | ||||
| Abstract | ||||
| 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. | ||||
| Keywords | ||||
| Dry reforming; Supports; Calcination temperature; Synthesis gas | ||||
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