The dehydrogenation of isobutane on a commercial chromia-alumina catalyst was studied using a conventional and a membrane reactor. A series of differential runs were conducted varying the temperature and feed composition. Extensive loss of catalyst activity was observed within the first two or three
Reaction assisted hydrogen transport during catalytic dehydrogenation in a membrane reactor
โ Scribed by E. Gobina; R. Hughes
- Publisher
- Elsevier Science
- Year
- 1996
- Tongue
- English
- Weight
- 557 KB
- Volume
- 137
- Category
- Article
- ISSN
- 0926-860X
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