Baffle effects on the performance of a catalytic circulating fluidized bed reactor were examined experimentally. The circulating fluidized bed reactor or riser was 102 mm in diameter and 6.32 m in height. Reaction was the catalytic decomposition of ozone using FCCparticles with a mean diameter of 89
Circulating fluidized bed as a catalytic reactor: Experimental study
β Scribed by S. Ouyang; X.-G. Li; O. E. Potter
- Publisher
- American Institute of Chemical Engineers
- Year
- 1995
- Tongue
- English
- Weight
- 896 KB
- Volume
- 41
- Category
- Article
- ISSN
- 0001-1541
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