DC Field | Value | Language |
---|---|---|
dc.contributor.author | Kim, Sang Done | - |
dc.contributor.author | Baker, C.G.J. | - |
dc.contributor.author | Bergougnou, M.A. | - |
dc.date.accessioned | 2008-07-14T01:27:13Z | - |
dc.date.available | 2008-07-14T01:27:13Z | - |
dc.date.issued | 1975 | - |
dc.identifier.citation | Can. J. Chem. Eng. 53, pp. 134-139 | en |
dc.identifier.issn | 0008-4034 | - |
dc.identifier.uri | http://www.cheminst.ca/index.cfm/ci_id/1130/la_id/1.htm | - |
dc.identifier.uri | http://hdl.handle.net/10203/5686 | - |
dc.description.abstract | The individual phase holdups in two (liquid-air, liquid-solids)and three (liquid-air-solids) phase fluidized beds have been measured ovr a wide range of liquid and gas velocities. Experiments were carried out in a large two-dimensional bed. Three solids were used ranging in size from 1 to 6 mm. The effect of viscosity (1-70 cp) was determined using solution of sugar and carboxymethyl cellulose of different concentrations. Various acetone tension in the range 44-73 dyne/cm. Beds of particles having a minimum fluidzing velocity in the liquid of less than 1.28cm/s were found to initially contract upon the injection of gas In contrast, beds of particles having minimum fluidizing velocitiess excedding this value were found to expand | en |
dc.language.iso | en_US | en |
dc.publisher | Canadian Society for Chemical Engineering | en |
dc.title | Phase holdup characteristics of three phase fluidized beds | en |
dc.type | Article | en |
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