The influence of fines size distribution on them behaviour of gas fluidized beds at high temperature

被引:29
作者
Bruni, Giovanna
Lettieri, Paola
Newton, David
Yates, John
机构
[1] UCL, Dept Chem Engn, London WC1E 7JE, England
[2] BP Chem Ltd, Sunbury On Thames TW16 7LL, Middx, England
基金
英国工程与自然科学研究理事会;
关键词
gas fluidized beds; distribution; fluidization; temperature; expansion; collapse;
D O I
10.1016/j.powtec.2006.01.007
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper reports some of the results obtained from an extensive experimental campaign, aimed at, studying the influence on fluidization, of changing the size distribution of the fine sub-cuts (particles below 45 gm) of Group: A powders, with increasing, temperature:, The fluidization; behaviour of an alumina powder was monitored at temperatures ranging from ambient to 400 degrees C and by adding,to the, material previously deprived of fines two fine sub-cuts of nominal size 0-25 and 25-45 mu m, respectively. In the study presented here the total fines content was kept at 22% by weight for both powders. Results were obtained by performing. fluidization, tests such as bed, collapsed test,. pressure, drop profiles and bed expansion profiles. From the bed collapse test, the influence of fines on the fluidization behaviour-of the alumina was analysed and a comparison between the powders was drawn, in terms of dense phase, collapse rate, standardised, collapse time and bed expansion ratio. The validity of some classical equations used for describing the fluidization behaviour of powders, namely the Richardson-Zaki equation, was tested for the expansion and the collapse experiments. (C) 2006 Published by Elsevier B.V.
引用
收藏
页码:88 / 97
页数:10
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