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Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/301

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contributor.authorSingh, R K-
date.accessioned2006-07-01T04:01:10Z-
date.available2006-07-01T04:01:10Z-
date.issued2006-
identifier.citationChemical Engineering World, Jan 2006, P 38-42en
identifier.urihttp://hdl.handle.net/2080/301-
descriptionCopyright of the published version belongs to Publisheren
description.abstractFluidization as an established fluid-solid contacting technique has found extensive applications in unit operations like drying, adsorption and in chemical processes Viz. solid-catalized reactions, carbonization, gasification and combustion. A fluidized bed can be achieved by increasing the upward velocity of the fluid through a fixed bed. Fluidized bed technique as compared to fixed bed has specific advantages. Albeit many advantages claimed of fluidization, the efficiency and the quality in large scale and deep gas-solid beds are seriously affected by bubbling, channeling and slugging behaviors, resulting in poor gas-solid contact, lower diffusion and heat transfer rates.en
format.extent120260 bytes-
format.mimetypeapplication/pdf-
language.isoen-
titleHydrodynamic Studies of Gas-Solid Fluidization in Square Bed for Non-spherical Particlesen
typeArticleen
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