## Abstract Liquid‐phase volumetric mass transfer coefficients, __k__~L~a were determined in three‐phase inverse fluidized beds of low‐density polyethylene (LDPE) and polypropylene (PP) spheres fluidized by a countercurrent flow of air and Newtonian (water and glycerol solutions) or non‐Newtonian l
✦ LIBER ✦
Effect of reactor diameter on gas-liquid mass transfer in three-phase fluidized beds
✍ Scribed by K. Nguyen-Tien; A. Schumpe; W.-D. Deckwer
- Publisher
- American Institute of Chemical Engineers
- Year
- 1985
- Tongue
- English
- Weight
- 250 KB
- Volume
- 31
- Category
- Article
- ISSN
- 0001-1541
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