Please use this identifier to cite or link to this item: https://doi.org/10.1007/BF00813687
Title: Interphase fluid-particle mass transport at low Reynolds numbers
Authors: Hidajat, K. 
Aracil, D.J.
Carberry, J.J.
Kenney, C.N.
Keywords: interphase fluid mechanics
low Reynolds numbers
mass transport
Issue Date: Mar-1994
Source: Hidajat, K., Aracil, D.J., Carberry, J.J., Kenney, C.N. (1994-03). Interphase fluid-particle mass transport at low Reynolds numbers. Catalysis Letters 30 (1-4) : 213-217. ScholarBank@NUS Repository. https://doi.org/10.1007/BF00813687
Abstract: Industrial scale fixed bed processes are largely conducted at modest to high values of the particle Reynolds number. Laboratory fluid-solid fixed bed studies, including catalyst rate measurements, are carried out often at Rep < 0.1, a flow regime largely devoid of fluid-particle transport data and correlations. From a study of methyl iodide adsorption over charcoal it is shown that it is possible to use the transient breakthrough behaviour of a well-mixed recycle absorber to analyse gas-particle film coefficients where standard experimental models are not effective. © 1995 J.C. Baltzer AG, Science Publishers.
Source Title: Catalysis Letters
URI: http://scholarbank.nus.edu.sg/handle/10635/91526
ISSN: 1011372X
DOI: 10.1007/BF00813687
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