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Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/993

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contributor.authorKumar, A-
contributor.authorRoy, G K-
date.accessioned2009-08-03T09:43:11Z-
date.available2009-08-03T09:43:11Z-
date.issued2002-
identifier.citationPowder Technology,126, Pages 91-95, 2002en
identifier.urihttp://hdl.handle.net/2080/993-
description.abstractBed expansion data were obtained for unbaffled and two different types of baffled (coaxial rod and coaxial blade) gas-solid fluidized beds for varying operating parameters: fluid mass velocity, particle size, density and initial static bed heights. Correlations have been developed for the prediction of bed expansion. For this, the values of minimum fluidization mass velocity and settling mass velocity (Gs, considered as hindered settling) have been calculated with the help of available equations. The correlations developed are modified versions of those of Beranek and Sokol, where mass velocity ratio has been used in place of velocityen
format.extent140228 bytes-
format.mimetypeapplication/pdf-
language.isoen-
publisherElsevieren
titleInfluence of Coaxial-Rod- and Coaxial-Blade-Type Baffles on Bed Expansion in Gas-Solid Fluidizationen
typeArticleen
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