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THREE-PHASE FLUIDIZED BEDS WITH VISCOUS LIQUID: HYDRODYNAMICS AND MASS TRANSFER†

 

作者: A.N. PATWARI,   K. NGUYEN-TIEN,   A. SCHUMPE,   W.-D. DECKWER,  

 

期刊: Chemical Engineering Communications  (Taylor Available online 1986)
卷期: Volume 40, issue 1-6  

页码: 49-65

 

ISSN:0098-6445

 

年代: 1986

 

DOI:10.1080/00986448608911690

 

出版商: Taylor & Francis Group

 

关键词: Three-phase fluidization;Hold-up;Mass transfer;Viscosity;Effective shear rate

 

数据来源: Taylor

 

摘要:

Hydrodynamics and gas/fiquid mass transfer in fluidized beds of glass spheres (3–8 mm diameter)were studied employing viscous aqueous solutions (16–53 mPas) Increasing liquid viscosity reduced the bubble disintegration capability of the particle beds. The most pronounced consequence was a strong decrease in the volumetric mass transfer coefficients (kLa) From a comparison of kLa in Newtonian and pseudoplastic liquids it is concluded that the effective shear rates in three-phase fluidized beds are higher than in bubble columns.

 

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