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Mass transfer from fluid and solid spheres at low reynolds numbers

 

作者: C. W. Bowman,   D. M. Ward,   A. I. Johnson,   O. Trass,  

 

期刊: The Canadian Journal of Chemical Engineering  (WILEY Available online 1961)
卷期: Volume 39, issue 1  

页码: 9-13

 

ISSN:0008-4034

 

年代: 1961

 

DOI:10.1002/cjce.5450390104

 

出版商: Wiley Subscription Services, Inc., A Wiley Company

 

数据来源: WILEY

 

摘要:

AbstractPredicted continuous phase mass transfer coefficients for fluid and solid spheres in the Stokes region of flow are correlated as Sherwood numbers plotted against Peclet numbers. These correlations permit a study of the effect of internal circulation on the rate of mass transfer from fluid spheres. At a Peclet number of 104, the theory predicts a threefold increase in transfer due to the circulation movements within a gas bubble. At a Peclet number below 10−2, the difference between a circulating and non‐circulating (or solid) sphere is indiscernible.The analysis presented in this paper for fluid spheres is based on a study by Friedlander(1)of mass transfer around solid spheres. A more elaborate concentration profile through the boundary layer has been used in the present investigation and the result reported for solid spheres differs about 8% from that given by Friedlander.The more interesting details of the mathematical treatment and the machine computation of the resulting differential equations are inclu

 

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