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|Title:||Interphase fluid-particle mass transport at low Reynolds numbers||Authors:||Hidajat, K.
|Keywords:||interphase fluid mechanics
low Reynolds numbers
|Issue Date:||Mar-1994||Citation:||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|
|Appears in Collections:||Staff Publications|
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