The minimum bubbling velocity of fluidized beds operating at high temperature

被引:39
作者
Girimonte, R. [1 ]
Formisani, B. [1 ]
机构
[1] Univ Calabria, Dipartimento Ingn Chim & Mat, I-87030 Cosenza, Italy
关键词
Fluidization; High temperature; Minimum bubbling velocity; Interparticle forces; Bed voidage; Expansion diagram; FINE POWDERS; INCIPIENT FLUIDIZATION; INTERPARTICLE FORCES; SIZE DISTRIBUTION; DENSE PHASE; BEHAVIOR; PRESSURE; VOIDAGE; SOLIDS;
D O I
10.1016/j.powtec.2008.06.006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The paper studies the influence of operating temperature oil the transition of a fluidized bed to the bubbling regime. Fluidization experiments and collapse tests were performed in a 54mm W. transparent column on samples of FCC, silica sand and corundum, at temperatures ranging from 30 to 500 degrees C. All the solids investigated, included in group A of Geldart classification, exhibited homogeneous expansion after fluidization at all temperatures. Depending on the technique adopted to identify the velocity at which the bed enters the bubbling regime, different trends of u(mb) versus T are observed. Such results are analysed together with the expansion behaviour of particle systems of various densities, illustrated by diagrams built with data of fluidization and collapse experiments. The role exerted by thermally induced interparticle forces in delaying the onset of steady bubbling is highlighted, as well as the opportunity of adopting a definition of U-mb of practical meaning. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:74 / 81
页数:8
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