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
โฆ LIBER โฆ
Bubble size variation in two-phase models of fluidized bed reactors
โ Scribed by C. Fryer; O.E. Potter
- Book ID
- 118968602
- Publisher
- Elsevier Science
- Year
- 1972
- Tongue
- English
- Weight
- 537 KB
- Volume
- 6
- Category
- Article
- ISSN
- 0032-5910
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## Abstract Modeling and measurement of bubble size in a rotating fluidized bed (RFB) is described. A novel model of bubble growth has been proposed based on a bubble coalescence model by Darton et al. We modified the model according to the following concepts: (i) local centrifugal acceleration and