ON THE INCIPIENT FLUIDIZED STATE OF SOLID PARTICLES

被引:26
作者
HARTMAN, M [1 ]
COUGHLIN, RW [1 ]
机构
[1] UNIV CONNECTICUT, DEPT CHEM ENGN, STORRS, CT 06269 USA
关键词
D O I
10.1135/cccc19931213
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A comprehensive study has been reported on all aspects of the transition of packed bed to the state of incipient fluidization (point of minimum fluidization, onset of fluidization): particle size and shape, size distribution in a batch of particles, fixed bed voidage, pressure drop through a packed bed and onset of fluidization. A number of predictive equations have been compared that were proposed to estimate the minimum fluidization velocity. All the equations tested do not have any flow limitations and are applicable to laminar, transitional as well as to turbulent flow regime. While some equations have some foundation in theory, the other are more or less generalized correlations of experimental data amassed by different authors under various conditions. The influence of temperature and pressure on the minimum fluidization velocity has been explored with respect to the important applications such as combustion and gasification. Problems have also been discussed with transition from fixed to fluidized bed of binary and polydisperse systems.
引用
收藏
页码:1213 / 1241
页数:29
相关论文
共 71 条
[1]   BEHAVIOR OF GAS-FLUIDIZED BEDS OF FINE POWDERS .1. HOMOGENEOUS EXPANSION [J].
ABRAHAMSEN, AR ;
GELDART, D .
POWDER TECHNOLOGY, 1980, 26 (01) :35-46
[2]  
BIN AK, 1985, CHEM ENG SCI, V40, P2004, DOI 10.1016/0009-2509(85)80149-4
[3]  
Biswal K.C., 1984, J I ENG, V65, P15
[4]   PREDICTION OF MINIMUM FLUIDIZATION VELOCITY FOR GAS SOLID FLUIDIZATION OF REGULAR PARTICLES IN CONICAL VESSELS [J].
BISWAL, KC ;
BHOWMIK, T ;
ROY, GK .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1985, 30 (01) :57-62
[5]   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
[6]   THE EFFECT OF TEMPERATURE ON FLUIDIZED-BED BEHAVIOR [J].
BOTTERILL, JSM ;
TEOMAN, Y ;
YUREGIR, KR .
CHEMICAL ENGINEERING COMMUNICATIONS, 1982, 15 (1-4) :227-238
[7]   ONSET OF FLUIDIZATION AND SLUGGING IN BEDS OF UNIFORM PARTICLES [J].
BROADHURST, TE ;
BECKER, HA .
AICHE JOURNAL, 1975, 21 (02) :238-247
[8]  
BROWNELL LE, 1950, CHEM ENG PROG, V46, P415
[9]   Gas flow through packed columns [J].
Burke, SP ;
Plummer, WB .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1928, 20 (01) :1196-1200
[10]  
Carman P.C., 1937, T I CHEM ENG-LOND, V15, P156, DOI [10.1016/S0263-8762(97)80003-2, DOI 10.1016/S0263-8762(97)80003-2]