Effects of binary particle size distribution on the fluid dynamic behavior of fluidized, vibrated and vibrofluidized beds

被引:17
作者
Daleffe, R. V. [1 ]
Ferreira, M. C. [1 ]
Freire, J. T. [1 ]
机构
[1] Univ Fed Sao Carlos, PPGEQ, Programa Pos Grad Engn Quim, BR-13565905 Sao Carlos, SP, Brazil
关键词
vibrofluidized bed; vibrated bed; fluidized bed; fluidization; particle size distribution; size segregation;
D O I
10.1590/S0104-66322008000100010
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work the effects of particle size distribution on the dynamics and segregation patterns in fluidized, vibrated and vibrofluidized beds were investigated. A binary particle size distribution and a reference one composed of glass spheres with a mean Sauter diameter of 2.18 x 10(-3) m were tested. The experimental setup consisted basically of a circular glass chamber with a height of 0.50 m and a diameter of 0.114 m, operated in the fluidized bed mode (Gamma = 0.00), in either vibrated or vibrofluidized bed modes (Gamma = 2.00). The pressure drops in the fluidized and vibrofluidized beds were not significantly affected by the binary particle size distribution. Well-defined segregation patterns occurred in fluidized and vibrated beds with small particles concentrating at the top and large particles at the bottom in the first situation and the reverse in the second one. Segregation patterns in vibrofluidized beds depended on the values of vibration parameters. Segregation in vibrofluidized and vibrated beds was minimized by operating at a high amplitude of vibration.
引用
收藏
页码:83 / 94
页数:12
相关论文
共 27 条
[1]   SOLIDS MIXING IN VIBRATING PARTICLE BEDS - EFFECT OF A TUBE SUBMERGED IN THE BED [J].
AKIYAMA, T ;
NISHIYAMA, R .
POWDER TECHNOLOGY, 1994, 80 (01) :11-16
[2]   Stability of spouting regimes in conical spouted beds with inert particle mixtures [J].
Bacelos, MS ;
Freire, JT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (02) :808-817
[3]   OBSERVATIONS ON THE MECHANISMS OF SEGREGATION IN FLOTSAM-RICH, FULLY FLUIDIZED-BEDS [J].
BEECKMANS, JM ;
NILSSON, J ;
LARGE, JF .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1985, 24 (01) :90-95
[4]  
BRATU E, 1971, BRIT CHEM ENG PR TEC, V16, P691
[5]   FUNDAMENTAL POWDER MIXING MECHANISMS [J].
BRIDGWATER, J .
POWDER TECHNOLOGY, 1976, 15 (02) :215-236
[6]   PARTICLE AGGLOMERATION CHARACTERISTICS IN VIBRO-FLUIDIZED BED DRYERS [J].
CHEN, YL ;
LIN, PS ;
PENG, YL .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1991, 24 (05) :669-673
[7]  
CHEUNG L, 1974, CHEM ENG SCI, V29, P1301
[8]   MEASUREMENT OF SOLID EXCHANGE BETWEEN THE BUBBLE WAKE AND THE EMULSION PHASE IN A 3-DIMENSIONAL GAS-FLUIDIZED BED [J].
CHIBA, S ;
TANIMOTO, H ;
KOBAYASHI, H ;
CHIBA, T .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1979, 12 (01) :43-45
[9]   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
[10]   Analysis of the fluid-dynamic behavior of fluidized and vibrofluidized bed containing glycerol [J].
Daleffe, RV ;
Freire, JT .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2004, 21 (01) :35-46