Bubble phenomena in aerated vibrated beds of small particles

被引:21
作者
Eccles, ERA [1 ]
Mujumdar, AS [1 ]
机构
[1] MCGILL UNIV,DEPT CHEM ENGN,MONTREAL,PQ,CANADA
关键词
resonance; fine particles; vibration; bubble frequency; rise velocity;
D O I
10.1080/07373939708917220
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Beds of various model particles were vibrated vertically at frequencies varying from 0-25 Hz and half-amplitudes from 0-4 mm. Alumina, glass and molecular sieve particles (27 mu m to 1400 mu m) were used as model particles. Air flow rates varied from 0 to 3 times the minimum fluidizing velocity through a single slot, a single central orifice or a multiplicity of orifices in the supporting bottom plate. With increasing vibration frequency, the bubble size was found to attain a maximum while the bubble rise velocity and frequency reach minima at the resonance point which is achieved only in vibrated beds of fine particles (d(p) <150 mu m). At the resonant point, bubble sizes are up to 215% their value in the absence of vibration. On the other hand, bubble frequencies and bubble rise velocities are up to 75% lower than their values in the absence of vibration.
引用
收藏
页码:95 / 116
页数:22
相关论文
共 18 条
[1]  
CHEREMISSINOFF NP, 1984, HYDRODYNAMICS GAS SO
[2]  
Davidson J.F., 1963, FLUIDIZED PARTICLES
[3]  
ECCLES ERA, 1990, THESIS MCGILL U MONT
[4]  
ECCLES ERA, 1989, P 6 ENG C FLUID ENG, P219
[5]  
GELPERIN NI, 1967, OSZNOVITEKHNIKI PSEV
[6]   AERODYNAMICS OF A VIBRATED FLUID BED [J].
GUPTA, R ;
MUJUMDAR, AS .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1980, 58 (03) :332-338
[7]  
GUPTA R, 1979, THESIS MCGILL U MONT
[8]  
HARRISON D, 1961, T I CHEM ENG, V39
[9]  
Hiby J. W., 1967, P INT S FLUID NETH U, P99
[10]  
Kunii D., 1967, PROC INT S FLUIDIZAT, P243