The effect of bubble growth by coalescence on predictions of reactant conversion in a fluidized bed catalytic reactor has been investigated for reactions that are described by either Langmuir-Hinshelwood or a simple first order kinetics. The two-phase model of Orcutt et nl. with continuous change of
The effect of particle size distribution on the performance of a catalytic fluidized bed reactor
β Scribed by Guanglin Sun; John R. Grace
- Publisher
- Elsevier Science
- Year
- 1990
- Tongue
- English
- Weight
- 579 KB
- Volume
- 45
- Category
- Article
- ISSN
- 0009-2509
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