Transition from turbulent to fast fluidization

被引:5
作者
Bi, HT [1 ]
机构
[1] Univ British Columbia, Dept Biol & Chem Engn, Vancouver, BC V6T 1Z4, Canada
关键词
fast fluidization; flow regime; transport velocity; entrainment;
D O I
10.1080/00986440213131
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Based on eight transition criteria, at least two types of transition velocities are identified for the demarcation of the transition from turbulent to fast fluidization. The "critical velocity," U-se , corresponds to the significant entrainment of particles from the bed, beyond which a circulating fluidized bed operation becomes essential. The "transport velocity," U-tr , defines the transition to fast fluidization based on the axial solids concentration profiles. Below this velocity, a distinct interface exists between a top dilute region and a bottom dense region. Above U-tr , the variation of voidage with height becomes relatively smooth. U-tr is found to be a function of measurement location and riser height, as well as gas and particle properties.
引用
收藏
页码:942 / 958
页数:17
相关论文
共 23 条
[1]   A PROCEDURE TO DETERMINE PARTICLE AGGLOMERATION IN A FLUIDIZED-BED AND ITS EFFECT ON ENTRAINMENT [J].
BENONI, D ;
BRIENS, CL ;
BARON, T ;
DUCHESNE, E ;
KNOWLTON, TM .
POWDER TECHNOLOGY, 1994, 78 (01) :33-42
[2]  
Bi H.T., 1991, AICHE ANN M
[3]  
BI HT, 1995, CHEM ENG RES DES, V73, P154
[4]   PREDICTION OF ENTRAINMENT FROM GAS SOLID FLUIDIZED-BEDS [J].
BRIENS, CL ;
BERGOUGNOU, MA ;
BARON, T .
POWDER TECHNOLOGY, 1988, 54 (03) :183-196
[5]  
CHEN BY, 1980, CHEM METALLURGY, V5, P30
[6]  
CHEN TP, 1978, FLUIDIZATION, P151
[7]   Correlation on the particle entrainment rate in gas fluidized beds [J].
Choi, JH ;
Chang, IY ;
Shun, DW ;
Yi, CK ;
Son, JE ;
Kim, SD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (06) :2491-2496
[8]  
Geldart D., 1986, Gas Fluidization Technology, P123
[9]  
Han G. Y., 1985, Korean Journal of Chemical Engineering, V2, P141
[10]   ON THE NATURE OF TURBULENT AND FAST FLUIDIZED-BEDS [J].
HORIO, M ;
ISHII, H ;
NISHIMURO, M .
POWDER TECHNOLOGY, 1992, 70 (03) :229-236