On the capacity of continuous powder classification in a gas-fluidized bed with horizontal sieve-like baffles

被引:17
作者
Bosma, JC
Hoffmann, AC
机构
[1] Univ Groningen, Dept Ind Pharm, NL-9713 AV Groningen, Netherlands
[2] Univ Bergen, Dept Phys, Program Proc Technol, N-5007 Bergen, Norway
关键词
rate of segregation; horizontal baffles; fluidized beds; particle classification; capacity;
D O I
10.1016/S0032-5910(03)00097-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Using horizontal sieve-like baffles in fluidized beds increases the tendency of particle mixtures to segregate. This may be utilized to devise a new process for dry classification of particles according to size or density. To predict the capacity of a continuous classification process based on this principle, the segregation rate must be known in addition to the final concentration profile. This paper describes an experimental investigation of this, using a fluidized bed with horizontal sieve-like baffles and an equal density mixture. The experiments confirmed that the baffles increase the particle segregation in the bed, and hence, the purity of the flotsam in the top layer. The capacity of a continuous fluidized bed particle classifier and the effect of particle size on the obtainable segregation are discussed. A first modelling attempt to describe the rate of growth of the lower segregation layer is presented. The mechanistic model for axial particle transport proposed in the literature is only partially successful in explaining the experimental results. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 15
页数:15
相关论文
共 27 条
[1]   VERIFICATION OF MODELS AND CORRELATIONS FOR BUBBLE PROPERTIES IN FLUIDIZED-BEDS [J].
BARON, T ;
BRIENS, CL ;
GALTIER, P ;
BERGOUGNOU, MA .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (08) :2227-2233
[2]  
BOSMA JC, UNPUB CHEM ENG SCI
[3]   Central difference solutions of the kinematic model of settling of polydisperse suspensions and three-dimensional particle-scale simulations [J].
Bürger, R ;
Fjelde, KK ;
Höfler, K ;
Karlsen, KH .
JOURNAL OF ENGINEERING MATHEMATICS, 2001, 41 (2-3) :167-187
[4]  
CHEUNG L, 1974, CHEM ENG SCI, V29, P1301
[5]   FLUIDIZED BINARY-MIXTURES IN WHICH THE DENSER COMPONENT MAY BE FLOTSAM [J].
CHIBA, S ;
NIENOW, AW ;
CHIBA, T ;
KOBAYASHI, H .
POWDER TECHNOLOGY, 1980, 26 (01) :1-10
[6]  
DARTON RC, 1977, T I CHEM ENG-LOND, V55, P134
[7]  
DECHSIRI C, 2001, P PARTEC 2001 INT C
[8]   EFFECT OF PARTICLE-SIZE AND SIZE DISTRIBUTION ON BEHAVIOR OF GAS-FLUIDIZED BEDS [J].
GELDART, D .
POWDER TECHNOLOGY, 1972, 6 (04) :201-&
[9]  
Geldart D, 1992, Mixing in the Process Industries, V2, P62, DOI 10.1016/B978-075063760-2/50025-1
[10]   MODEL FOR A SEGREGATING GAS FLUIDIZED-BED [J].
GIBILARO, LG ;
ROWE, PN .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (06) :1403-1412