Prediction of Agglomerate Size for Fine Particles in a Vibro-fluidized Bed

A model for estimating the agglomerate size of Geldart group C powder in a vibro-fluidized bed was proposed. The agglomerate size was estimated by using the experimental value of the lower limit of gas velocity for channel breakage, ucha, and the void fraction, echa, at ucha. The force balance between cohesive force (van der Waals force) and separation force (gravity, vibration and shear force by a gas flow) was considered. The vibrational force was considered to act on the agglomerates to increase the effect of gravitational force. The calculated agglomerate size decreased with increasing vibration strength.The value of ucha decreased with increasing vibration strength for all tested group C powders in this study. The effects of particle properties such as particle diameter, density and material on ucha were discussed. It was found that a higher value of ucha was obtained when the cohesive force was large in the cohesive-separation force balance. This indicates the particle properties affect the cohesive–separation force balance.

[1]  S. Uchida,et al.  Effect of particle diameter on fluidization under vibration , 2002 .

[2]  Alex C. Hoffmann,et al.  The effect of vibration on the fluidization behaviour of some cohesive powders , 1994 .

[3]  Jamal Chaouki,et al.  Effect of interparticle forces on the hydrodynamic behaviour of fluidized aerogels , 1985 .

[4]  L. G. Gibilaro,et al.  A fully predictive criterion for the transition between particulate and aggregate fluidization , 1984 .

[5]  J. Israelachvili Intermolecular and surface forces , 1985 .

[6]  S. Mori Vibro-fluidization of group-C particles and its industrial applications , 1990 .

[7]  Katsuki Kusakabe,et al.  FLUIDIZATION STATE OF ULTRAFINE POWDERS , 1988 .

[8]  The Fluidization of Fine Particles under Vibrated or Reduced Pressure Conditions , 1997 .

[9]  Alvin W. Nienow,et al.  Fluidisation of fine and very dense hardmetal powders , 1990 .

[10]  O. Molerus,et al.  Interpretation of Geldart's type A, B, C and D powders by taking into account interparticle cohesion forces , 1982 .

[11]  Katsuji Noda,et al.  Comparison of three vibrational modes (twist, vertical and horizontal) for fluidization of fine particles , 2001 .

[12]  Tao Zhou,et al.  Force balance modelling for agglomerating fluidization of cohesive particles , 2000 .

[13]  Tao Zhou,et al.  Estimation of agglomerate size for cohesive particles during fluidization , 1999 .

[14]  S. George,et al.  Vibro-fluidization of fine boron nitride powder at low pressure , 2001 .

[15]  Hiroyuki Hatano,et al.  Fluidization of Ultrafine Particles with High G , 2001 .

[16]  Henry Shaw,et al.  Gas–solid fluidization in a centrifugal field , 2001 .

[17]  D. Geldart Types of gas fluidization , 1973 .

[18]  Masayuki Horio,et al.  Prediction of agglomerate sizes in bubbling fluidized beds of group C powders , 1998 .

[19]  E. Stamhuis,et al.  Fluidization of potato starch in a stirred vibrating fluidized bed , 1996 .

[20]  Shigeo Uchida,et al.  Flow Patterns of Fine Particles in a Vibrated Fluidized Bed under Atmospheric or Reduced Pressure , 1998 .