An investigation of the effect of the interparticle forces on the fluidization behaviour of fine powders linked with rheological studies

被引:59
作者
Bruni, Giovanna
Lettieri, Paola
Newton, David
Barletta, Diego
机构
[1] UCL, Dept Chem Engn, London WC1E 7JE, England
[2] BP Chem Ltd, Sunbury Of Thames TW16 7LL, Middx, England
[3] Univ Salerno, Dipartimento Ingn Chim & Alimentare, I-84084 Fisciano, SA, Italy
基金
英国工程与自然科学研究理事会;
关键词
fluidization; fines; temperature; rheology; failure properties;
D O I
10.1016/j.ces.2006.08.059
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper reports on an extensive experimental campaign aimed at studying the influence of interparticle forces on the fluidization behaviour of fine group A powders by changing the size distribution of the fine sub-cuts (particles below 45 mu m) and with increasing temperature. The fluidization behaviour of an alumina powder was investigated at temperatures ranging from ambient up to 400 degrees C and by adding to the material previously deprived of fines two fine sub-cuts of nominal size 0-25 mu m and 25-45 mu m, respectively. Four samples were investigated, containing 22% and 30% wt of fines and having similar particle size distribution but shifted towards smaller and bigger fines sub cuts. Fluidization and rheological tests were performed in parallel. Results obtained from pressure drop profiles, bed expansion profiles and bed collapse test were linked to the rheological analysis of the failure properties of the materials. The static angle of internal friction phi, the effective angle of internal friction phi(e), cohesion C, the angle of wall friction phi(w) and wall adhesion A, the dynamic angle of internal friction delta and dynamic cohesion C(delta) were determined to underpin the role of the interparticle forces on the ability of the powders to flow and to their fluidization quality when adding small or big fines to the material. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:387 / 396
页数:10
相关论文
共 39 条
[1]   BEHAVIOR OF GAS-FLUIDIZED BEDS OF FINE POWDERS .2. VOIDAGE OF THE DENSE PHASE IN BUBBLING BEDS [J].
ABRAHAMSEN, AR ;
GELDART, D .
POWDER TECHNOLOGY, 1980, 26 (01) :47-55
[2]  
BARLETTA D, 2005, POWDERS GRAINS 2005, P1033
[3]   THE MEASUREMENT OF EMULSION PHASE VOIDAGE IN GAS-FLUIDIZED BEDS OF FINE POWDERS [J].
BARRETO, GF ;
YATES, JG ;
ROWE, PN .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (03) :345-350
[4]   THE EFFECT OF OPERATING TEMPERATURE ON THE VELOCITY OF MINIMUM FLUIDIZATION, BED VOIDAGE AND GENERAL BEHAVIOR [J].
BOTTERILL, JSM ;
TEOMAN, Y ;
YUREGIR, KR .
POWDER TECHNOLOGY, 1982, 31 (01) :101-110
[5]  
BRUNI G, 2006, IN PRESS CHEM ENG SC, DOI DOI 10.1016/J.CES.2006.08.060
[6]  
Bruni G., 2005, THESIS U COLL LONDON
[7]   The influence of fines size distribution on them behaviour of gas fluidized beds at high temperature [J].
Bruni, Giovanna ;
Lettieri, Paola ;
Newton, David ;
Yates, John .
POWDER TECHNOLOGY, 2006, 163 (1-2) :88-97
[8]  
Carr R.L., 1965, Chem. Eng, V72, P163, DOI DOI 10.1016/J.JAEROSCI.2007.10.003
[9]   BUBBLE-FREE EXPANSION OF GAS-FLUIDIZED BEDS OF FINE PARTICLES [J].
DONSI, G ;
MASSIMILLA, L .
AICHE JOURNAL, 1973, 19 (06) :1104-1110
[10]  
FORMISANI B, 1998, CHEM ENG SCI, V39, P1667