Fluidization of Nano-size Particles

Fluidization and collapsing bed experiments were performed with 'Tullanox', 10 nm diameter fumed silica. The minimum fluidization velocity was determined to be 0.0115 m/s at the unusually low volume fraction of solids of 0.0077. The solids volume fraction was measured using a γ-ray densitometer. Fluidization was without large bubbles, with a high bed expansion ratio. The highest granular temperature was of the order of that of Geldart B particles, as measured by Cody et al. (1996). The sedimentation process was simulated using a two-fluid hydrodynamic model. The input into the model was a measured solids stress modulus and an agglomerate size determined from the settling curves. With these two rheological parameters, there was good agreement between the sedimentation theory and the experiment. This study shows that the standard collapse bed experiment used in industry is a good test of rheological properties of particles.

[1]  Mooson Kwauk,et al.  Fluidization of fine particles , 1998 .

[2]  Yong Jin,et al.  Unique properties of 30‐μm particles as the catalyst of fluidized‐bed reactors , 1997 .

[3]  Susan J. Gelderbloom,et al.  CFD Simulations of bubbling/collapsing fluidized beds for three Geldart Groups , 2003 .

[4]  Andrew N. Norris,et al.  Particle granular temperature in gas fluidized beds , 1996 .

[5]  Wei Fei,et al.  Fluidization and agglomerate structure of SiO2 nanoparticles , 2002 .

[6]  Dimitri Gidaspow,et al.  Computation of circulating fluidized-bed riser flow for the Fluidization VIII benchmark test , 1999 .

[7]  D. Wasan,et al.  Electrokinetic phenomena in the filtration of colloidal particles suspended in nonaqueous media , 1981 .

[8]  M. L. Laucks,et al.  Aerosol Technology Properties, Behavior, and Measurement of Airborne Particles , 2000 .

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

[10]  E. W. Grohse Analysis of gas-fluidized solid systems by x-ray absorption , 1955 .

[11]  D. Gidaspow Multiphase Flow and Fluidization: Continuum and Kinetic Theory Descriptions , 1994 .

[12]  Dimitri Gidaspow,et al.  Hydrodynamics of electroluidization: Separation of pyrites from coal , 1987 .

[13]  Dimitri Gidaspow,et al.  Collisional viscosity of FCC particles in a CFB , 1996 .

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

[15]  R. Jackson,et al.  The mechanics of gas fluidized beds with an interval of stable fluidization , 1993, Journal of Fluid Mechanics.

[16]  Dimitri Gidaspow,et al.  Electrostatic separation of powder mixtures based on the work functions of its constituents , 1993 .

[17]  R. Jackson,et al.  The Dynamics of Fluidized Particles , 2000 .

[18]  Dimitri Gidaspow,et al.  Fluidization in two-dimensional beds with a jet. 1. Experimental porosity distributions , 1983 .

[19]  J. Yates,et al.  The significance of bed collapse experiments in the characterization of fluidized beds of fine powders , 1988 .

[20]  Dimitri Gidaspow,et al.  An x-ray-. gamma. -ray method of measurement of binary solids concentrations and voids in fluidized beds , 1987 .

[21]  D. Jeffrey,et al.  Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flowfield , 1984, Journal of Fluid Mechanics.

[22]  D. Wasan,et al.  Sedimentation of fine particles in nonaqueous media: Part I — experimental Part II — modeling , 1986 .

[23]  S. L. Soo,et al.  Fluid dynamics of multiphase systems , 1967 .

[24]  R. B. Thorpe,et al.  Evaporation of water from air-fluidized porous particles , 2001 .