Fluidization of nano-size particles

被引:75
作者
Jung, JW [1 ]
Gidaspow, D [1 ]
机构
[1] IIT, Dept Environm Chem & Engn, Chicago, IL 60616 USA
关键词
collapsing bed; solids stress; computational fluid dynamics; two-fluid model;
D O I
10.1023/A:1022807918247
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
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 gamma-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.
引用
收藏
页码:483 / 497
页数:15
相关论文
共 36 条
[1]  
[Anonymous], FLUIDIZATION
[2]   THE SIGNIFICANCE OF BED COLLAPSE EXPERIMENTS IN THE CHARACTERIZATION OF FLUIDIZED-BEDS OF FINE POWDERS [J].
BARRETO, GF ;
MAZZA, GD ;
YATES, JG .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (11) :3037-3047
[3]  
Bird R.B., 2006, TRANSPORT PHENOMENA, Vsecond, DOI 10.1002/aic.690070245
[4]   ELECTROKINETIC PHENOMENA IN THE FILTRATION OF COLLOIDAL PARTICLES SUSPENDED IN NON-AQUEOUS MEDIA [J].
CHOWDIAH, P ;
WASAN, DT ;
GIDASPOW, D .
AICHE JOURNAL, 1981, 27 (06) :975-984
[5]   Particle granular temperature in gas fluidized beds [J].
Cody, GD ;
Goldfarb, DJ ;
Storch, GV ;
Norris, AN .
POWDER TECHNOLOGY, 1996, 87 (03) :211-232
[6]   Evaporation of water from air-fluidized porous particles [J].
Davidson, JF ;
Thorpe, RB ;
Al-Mansoori, O ;
Kwong, H ;
Peck, M ;
Williamson, R .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (21-22) :6089-6097
[7]   TYPES OF GAS FLUIDIZATION [J].
GELDART, D .
POWDER TECHNOLOGY, 1973, 7 (05) :285-292
[8]  
GELDERBLOOM SJ, 2001, THESIS ILLINOIS I TE
[9]  
GELDERBLOOM SJ, 2001, IN PRESS AICHE J
[10]   FLUIDIZATION IN TWO-DIMENSIONAL BEDS WITH A JET .1. EXPERIMENTAL POROSITY DISTRIBUTIONS [J].
GIDASPOW, D ;
LIN, C ;
SEO, YC .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1983, 22 (02) :187-193