Hydrodynamics and heat transfer were investigated in a 0.28 m diameter slurry bubble column for air-water-yeast cells system. Yeast cells of about 8 m diameter were used and the effects of gas velocity and yeast concentrations were studied. Gas holdups exhibited a maximum value around a gas superfic
โฆ LIBER โฆ
Influence of bubble column diameter on local heat transfer and related hydrodynamics
โ Scribed by A.K. Jhawar; A. Prakash
- Book ID
- 113533353
- Publisher
- Institution of Chemical Engineers
- Year
- 2011
- Tongue
- English
- Weight
- 336 KB
- Volume
- 89
- Category
- Article
- ISSN
- 0263-8762
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## Scale-up Heat transfer coefficients were measured in fluidization columns of 0.29 m and 1.56 m ID at fixed distance above the distributor, using an identical vertical heater, the same alumina particles and geometrically scaled bubble-cap distributors. The magnitude of the maximum heat transfer
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