The expansion of gas-fluidised beds in bubbling fluidisation

被引:33
作者
Gunn, DJ [1 ]
Hilal, N [1 ]
机构
[1] UNIV COLL SWANSEA,DEPT CHEM ENGN,SWANSEA SA2 8PP,W GLAM,WALES
关键词
fluidisation; bubbling; solids holdup; expansion;
D O I
10.1016/S0009-2509(97)00051-1
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
The expansion of gas-fluidised beds has been examined in the range of Archimedes number from 100 to 10(5) using five grades of glass ballotini and two grades of lead shot of narrow size distribution, and Diakon particles of wide size distribution. A porous plastic distributor plate was used in beds of diameters 89 and 290 mm. Power law and exponential correlations of the expansion were examined. All of the experimental data were correlated within experimental error by the equation rho(b)/rho(mf) = exp[-0.0052U*(U/U-mf - 1)]. The dimensionless group U*, not apparently considered elsewhere, is defined as U-t(rho/mu g)(1/3) where U-t is the particle terminal velocity. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:2811 / 2822
页数:12
相关论文
共 16 条
[1]
EXPANSION CHARACTERISTICS OF A BUBBLING FLUIDIZED-BED [J].
BEST, RJ ;
YATES, JG .
POWDER TECHNOLOGY, 1977, 16 (02) :285-288
[2]
CANADA GS, 1978, AICHE S SER, V77, P14
[3]
LARGE PARTICLE FLUIDIZATION [J].
CRANFIELD, RR ;
GELDART, D .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (04) :935-947
[4]
de Groot J.H., 1967, P INT S FLUID, P348
[5]
FRANTZ JF, 1966, CHEM ENG PROG S SER, V62, P62
[6]
COMPARISON OF COMMONLY USED CORRELATIONS FOR MINIMUM FLUIDIZATION VELOCITY OF SMALL SOLID PARTICLES [J].
GREWAL, NS ;
SAXENA, SC .
POWDER TECHNOLOGY, 1980, 26 (02) :229-234
[7]
GREWAL NS, 1979, CHEM ENG J BIOCH ENG, V18, P197
[8]
HEAT-TRANSFER FROM VERTICAL SURFACES TO DENSE GAS-FLUIDIZED BEDS [J].
GUNN, DJ ;
HILAL, N .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1994, 37 (16) :2465-2473
[9]
JOVANOVIC G, 1979, THESIS OREGON STATE
[10]
THE RESISTANCE TO MOTION OF A SOLID SPHERE IN A FLUID [J].
KHAN, AR ;
RICHARDSON, JF .
CHEMICAL ENGINEERING COMMUNICATIONS, 1987, 62 (1-6) :135-150