DSpace@nitr: Item 2080/1050

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DC Field	Value	Language
contributor.author	Jena, H M	-
contributor.author	Roy, G K	-
contributor.author	Meikap, B C	-
date.accessioned	2009-09-23T04:09:32Z	-
date.available	2009-09-23T04:09:32Z	-
date.issued	2009	-
identifier.citation	Powder Technology (2009)	en
identifier.uri	http://dx.doi.org/10.1016/j.powtec.2009.07.022	-
identifier.uri	http://hdl.handle.net/2080/1050	-
description.abstract	Semi-fluidized bed hydrodynamics, including minimum and maximum semifluidization velocities, packed bed formation and pressure drop across the bed, have been studied in a 0.1 m ID liquid-solid semi-fluidized bed. The top grid is a specially designed perforated plate to have negligible pressure drop across it and to retain all the particles used in the experiment. Experimental parameters studied included velocity, density and viscosity of the liquid, particle size, static bed height and expansion ratio. Empirical and semi-empirical models have been derived. The results have been compared with those available in the literature.	en
format.extent	1328049 bytes	-
format.mimetype	application/pdf	-
language.iso	en	-
publisher	Elsevier	en
subject	Hydrodynamics	en
subject	Liquid-solid semi-fluidization	en
subject	Pressure drop	en
subject	packed bed height	en
subject	minimum and maximum semi-fluidization velocity	en
subject	viscosity effect.	en
title	Hydrodynamics of Regular Particles in a Liquid-Solid Semifluidized Bed	en
type	Article	en
Appears in Collections:	Journal Articles

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