## Abstract The effect of uniformity of fluidization on the catalytic cracking of cumene, with a silicaalumina catalyst, was studied in a 3βin.βdiameter reactor operated at 800Β°F. Superficial gas velocities were varied from 0.06 to 0.24 ft./sec. for bed heights of 1.5, 3, 5, and 8 in. The percentag
Effect of fluidization on catalytic cumene dealkylation
β Scribed by J. F. Mathis; C. C. Watson
- Publisher
- American Institute of Chemical Engineers
- Year
- 1956
- Tongue
- English
- Weight
- 904 KB
- Volume
- 2
- Category
- Article
- ISSN
- 0001-1541
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