Please use this identifier to cite or link to this item:
https://open.uns.ac.rs/handle/123456789/9898
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Bukur, Dragomir | en_US |
dc.date.accessioned | 2020-03-03T14:35:47Z | - |
dc.date.available | 2020-03-03T14:35:47Z | - |
dc.date.issued | 1978-01-01 | - |
dc.identifier.issn | 01964313 | en_US |
dc.identifier.uri | https://open.uns.ac.rs/handle/123456789/9898 | - |
dc.description.abstract | Gas flow distribution and the cross-sectional areas occupied by the bubble and particulate phases in a fluidized bed are examined for the models of Partridge and Rowe, Kunii and Levenspiel, and Fryer and Potter. It has been shown that for these models there exists a critical value of fluidizing gas velocity, defined as the gas velocity at which the area of one of the phases becomes equal to the total cross-sectional area of the bed. For a given set of model parameters the value of the critical fluidizing gas velocity can be predicted. Existence of such a critical velocity imposes restrictions on the applicability of these models. Some modifications of the Partridge-Rowe model are proposed in order to extend the region of validity of this model while retaining its basic features. © 1978, American Chemical Society. All rights reserved. | en |
dc.relation.ispartof | Industrial and Engineering Chemistry Fundamentals | en |
dc.title | Analysis of Gas Flow in Fluidized Bed Reactors | en_US |
dc.type | Journal/Magazine Article | en_US |
dc.identifier.doi | 10.1021/i160066a009 | - |
dc.identifier.scopus | 2-s2.0-0017968997 | - |
dc.identifier.url | https://api.elsevier.com/content/abstract/scopus_id/0017968997 | - |
dc.description.version | Unknown | en_US |
dc.relation.lastpage | 123 | en |
dc.relation.firstpage | 120 | en |
dc.relation.issue | 2 | en |
dc.relation.volume | 17 | en |
item.grantfulltext | none | - |
item.fulltext | No Fulltext | - |
Appears in Collections: | Naučne i umetničke publikacije |
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