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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