model for the operation of a continuously operating fluidised catalytic cracker is developed on the basis of the two-phase theory of fluidisation. The model also incorporates the decay in catalyst activity which is a feature of cracking processes; the mean catalyst activity is evaluated using the re
A revised model for predicting the performance of a fluidised-bed catalytic reactor
β Scribed by J. Pereira; K. Chandrasekharan; P.H. Calderbank
- Publisher
- Elsevier Science
- Year
- 1981
- Tongue
- English
- Weight
- 299 KB
- Volume
- 36
- Category
- Article
- ISSN
- 0009-2509
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