Parametric effects of particle size and gas velocity on cluster characteristics in fast fluidized beds
β Scribed by Arun K Sharma; Kemal Tuzla; John Matsen; John C Chen
- Book ID
- 114079155
- Publisher
- Elsevier Science
- Year
- 2000
- Tongue
- English
- Weight
- 303 KB
- Volume
- 111
- Category
- Article
- ISSN
- 0032-5910
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π SIMILAR VOLUMES
Static and dynamic bifurcation behaviors dominate the operation of fluidized bed catalytic reactors for the production of polyethylene (UNIPOL Process) and have important implications on the safe operating temperature and polyethylene production rate. The investigations show that the multiplicity of
The expansion of gas-liquid fluidized beds has been measured for beds of glass ballotini fluidized by air/water. Particle diameters varied from 0.28 to 2.2 mm, and settled bed heights from U-107 cm. The flow rates of air and water were varied independently. The expansion of a liquid fluidized bed i