Please use this identifier to cite or link to this item: https://doi.org/10.1007/BF00813687
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dc.titleInterphase fluid-particle mass transport at low Reynolds numbers
dc.contributor.authorHidajat, K.
dc.contributor.authorAracil, D.J.
dc.contributor.authorCarberry, J.J.
dc.contributor.authorKenney, C.N.
dc.date.accessioned2014-10-09T08:19:08Z
dc.date.available2014-10-09T08:19:08Z
dc.date.issued1994-03
dc.identifier.citationHidajat, 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
dc.identifier.issn1011372X
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/91526
dc.description.abstractIndustrial 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.
dc.description.urihttp://libproxy1.nus.edu.sg/login?url=http://dx.doi.org/10.1007/BF00813687
dc.sourceScopus
dc.subjectinterphase fluid mechanics
dc.subjectlow Reynolds numbers
dc.subjectmass transport
dc.typeArticle
dc.contributor.departmentCHEMICAL ENGINEERING
dc.description.doi10.1007/BF00813687
dc.description.sourcetitleCatalysis Letters
dc.description.volume30
dc.description.issue1-4
dc.description.page213-217
dc.description.codenCALEE
dc.identifier.isiutA1995QE23400021
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