Prediction of minimum fluidization velocity for fine tailings materials

被引:33
作者
Gupta, S. K. [1 ]
Agarwal, V. K. [2 ]
Singh, S. N. [3 ]
Seshadri, V. [3 ]
Mills, David [4 ]
Singh, J. [1 ]
Prakash, Chandra
机构
[1] Banaras Hindu Univ, Hydraul Engn Div, Dept Civil Engn, Inst Technol, Varanasi 221005, Uttar Pradesh, India
[2] Indian Inst Technol Delhi, ITMME Ctr, New Delhi, India
[3] Indian Inst Technol Delhi, Dept Appl Mech, New Delhi, India
[4] Glasgow Caledonian Univ, Glasgow G4 0BA, Lanark, Scotland
关键词
Gas-solid fluidization; Minimum fluidization velocity; Fluidized motion conveying system; Correlation; INTERPARTICLE FORCES; INCIPIENT FLUIDIZATION; ELEVATED-TEMPERATURES; PRESSURE-DROP; PARTICLE-SIZE; PHASE VOIDAGE; DENSE PHASE; GAS; BEDS; BUBBLE;
D O I
10.1016/j.powtec.2009.08.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The suitability of several minimum fluidization velocity correlations has been investigated for fine zinc slime, iron ore tailings, both pre and post hydro-cyclone uranium tailings, and a relatively coarse grade of fly ash. it has been found that most of the published correlations significantly underestimate the value of minimum fluidization velocity for the four different tailings materials. Predictions due to Van Heerden et al. (1951) [45], Noda et al. (1986) [76], Coltters and Rivas (2004) [39], and Xu and Zhu (2009) [93], agree reasonably with the experimental data, whereas the fly ash, which belongs to Geldart Group B materials, has shown a large deviation. Thus these correlations could be used for the fine tailings materials that comprise a variety of constituents and possess a degree of cohesiveness. A modification of Coltters and Rivas correlation has also been suggested to assess the combined effect of particle size and density on minimum fluidization velocity. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:263 / 271
页数:9
相关论文
共 96 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]   MINIMUM FLUIDIZATION VELOCITIES OF FLUIDIZED-BED COAL-COMBUSTION SOLIDS [J].
ADANEZ, J ;
ABANADES, JC .
POWDER TECHNOLOGY, 1991, 67 (02) :113-119
[3]  
ANDERSSON KEB, 1961, CHEM ENG SCI, V15, P276
[4]  
Babu S.P., 1978, AIChE Symp. Ser, V74, P176
[5]  
Baeyens J., 1973, Proc. Conf. La Fluidisation et ses Applications, Cepadues Editions, Toulouse, P226
[6]  
BARBOSA, 1995, FLUIDIZATION 8, V1, P145
[7]   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
[8]   PREDICTION OF THE MINIMUM FLUIDIZATION VELOCITY [J].
BIN, AK .
POWDER TECHNOLOGY, 1994, 81 (02) :197-199
[9]   RATIO OF TERMINAL VELOCITY TO MINIMUM FLUIDIZING VELOCITY FOR SPHERICAL PARTICLES [J].
BOURGEOIS, P ;
GRENIER, P .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1968, 46 (05) :325-+
[10]   ONSET OF FLUIDIZATION AND SLUGGING IN BEDS OF UNIFORM PARTICLES [J].
BROADHURST, TE ;
BECKER, HA .
AICHE JOURNAL, 1975, 21 (02) :238-247