Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/149
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dc.contributor.authorBiswal, K C-
dc.contributor.authorBhowmik, T-
dc.contributor.authorRoy, G K-
dc.date.accessioned2005-10-04T08:13:25Z-
dc.date.available2005-10-04T08:13:25Z-
dc.date.issued1985-
dc.identifier.citationThe Chemical Engineering Journal, Vol 30, Iss 1, P 57-62en
dc.identifier.urihttp://hdl.handle.net/2080/149-
dc.descriptioncopyright for this article belongs to Elsevier Science Ltden
dc.description.abstractThe application of a conical fluidized bed as a remedial measure for certain inherent drawbacks of gas-solid systems is suggested. Investigations were carried out in Perspex cones with apex angles of 10°, 30°, 45° and 60°, with spherical glass beads of different sizes as the bed material, and air as the fluidizing medium. With the help of available correlations and packed bed pressure drop data, minimum fluidization velocities for the above cases were computed and compared with experimental data obtained from bed pressure drop versus fluid mass velocity plots, and the mean and standard deviations were calculated.en
dc.format.extent579859 bytes-
dc.format.mimetypeapplication/pdf-
dc.language.isoen-
dc.publisherElsevieren
dc.subjectfluidized beden
dc.subjectfluidization velocitiesen
dc.titlePrediction of minimum fluidization velocity for gas-solid fluidization of regular particles in conical vesselsen
dc.typeArticleen
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