Improvement of the Fluidizability of Cohesive Powders through Mixing with Small Proportions of Group A Particles

The gas fluidization behaviour of fine cohesive powders, classified as Geldart group C, is known to be characterized by cracks and channels leading to severe non-homogeneities in the bed. Geldart group A particles, on the other hand, are known to show more homogeneous and regular fluidization behaviour. This paper studies the effects of the addition of small proportions of group A on the fluidization behaviour of a group C powder. Differential pressure fluctuations data at a sampling frequency of 200 Hz were recorded for two cases. In the first case, the bed contained only group C powder while in the second case small amounts of group A particles were added to the existing group C powder. Visual/image observations coupled with time series analysis showed that the addition of small proportions of group A particles substantially improved the fluidization behaviour of the bed even at low superficial gas velocities, leading to a more uniform fluidization. Evaluation of mean and standard deviations has shown the advantage of mixing the two powders as it allowed larger pressure fluctuations and smaller standard deviations. Power spectra, on the other hand, showed that unlike group C, for which fluctuations were small in magnitude and broadband in structure, the mixture showed stronger periodic behaviour as result of the attenuation of the small and rapid fluctuations caused by the flow of gas in the cracks and channels. Advanced methods such as the principal component analysis of the embedded trajectories allowed a quantitative comparison between the fluidization behaviour of the two systems.

[1]  L. T. Fan,et al.  Pressure fluctuations in a fluidized bed , 1981 .

[2]  Riccardo Chirone,et al.  Bubble-free fluidization of a cohesive powder in an acoustic field , 1993 .

[3]  Antonio Ramos,et al.  Flow Regimes in Fine Cohesive Powders , 1999 .

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

[5]  D. P. Skrzycke,et al.  Characterization of the fluidization behavior of different solid types based on chaotic time series analysis of pressure signals , 1993 .

[6]  Derek Geldart,et al.  Inter-particle forces in cohesive powders studied by AFM: effects of relative humidity, particle size and wall adhesion , 2003 .

[7]  H. Bi,et al.  Propagation of pressure waves and forced oscillations in gas-solid fluidized beds and their influence on diagnostics of local hydrodynamics , 1995 .

[8]  O. Levenspiel,et al.  Vibrating beds of fine particles: Estimation of interparticle forces from expansion and pressure drop experiments , 1992 .

[9]  John L. Casti Chaos data analyzer , 1996 .

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

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

[12]  A. Ajbar,et al.  Hydrodynamics of gas fluidized beds with mixture of group D and B particles , 2002 .

[13]  Derek Geldart,et al.  Fluidization of cohesive powders , 1984 .

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

[15]  M. Baerns EFFECT OF INTERPARTICLE ADHESIVE FORCES ON FLUIDIZATION OF FINE PARTICLES. , 1966 .

[16]  Masayuki Horio,et al.  A numerical study on agglomerate formation in a fluidized bed of fine cohesive particles , 2002 .

[17]  J. Visser,et al.  Van der Waals and other cohesive forces affecting powder fluidization , 1989 .

[18]  P. Rowe,et al.  Fine powders fluidised at low velocity at pressures up to 20 bar with gases of different viscosity , 1982 .

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

[20]  Nigel N. Clark,et al.  Local differential pressure analysis in a slugging bed using deterministic chaos theory , 1997 .

[21]  G. P. King,et al.  Extracting qualitative dynamics from experimental data , 1986 .

[22]  L. Drzal,et al.  Behavior of cohesive powders in narrow-diameter fluidized beds , 1989 .

[23]  C. S. Daw,et al.  Evaluation of control of fluidization quality through chaotic time series analysis of pressure-drop measurements , 1992 .

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

[25]  J. Chaouki,et al.  Hydrodynamic behaviour of aerogel powders in high-velocity fluidized beds , 1990 .

[26]  Daw,et al.  Chaotic characteristics of a complex gas-solids flow. , 1990, Physical review. A, Atomic, molecular, and optical physics.

[27]  P. N. Rowe,et al.  The bubbling behaviour of fine powders when fluidised , 1976 .

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

[29]  John R. Grace,et al.  Characterization of gas fluidized beds of group C, A and B particles based on pressure fluctuations , 1999 .

[30]  J. Chaouki,et al.  Improvement of the fluidisability of Ni/SiO2 aerogels by reducing interparticle forces , 1991 .

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

[32]  Hong-zhong Li,et al.  Effects of adding different size particles on fluidization of cohesive particles , 1999 .