DEM Analysis on Flow Patterns of Geldart's Group A Particles in Fluidized Bed

2002 ◽  
Vol 2002.3 (0) ◽  
pp. 307-308
Author(s):  
Tomonari KOBAYASHI ◽  
Toshihiro KAWAGUCHI ◽  
Toshitsugu TANAKA ◽  
Yutaka Tsuji
2001 ◽  
Vol 2001.76 (0) ◽  
pp. _12-3_-_12-4_
Author(s):  
Tetsuichiro MUKAI ◽  
Toshihiro KAWAGUCHI ◽  
Toshitsugu TANAKA ◽  
Yutaka TSUJI

2006 ◽  
Vol 43 (10) ◽  
pp. 737-745 ◽  
Author(s):  
Tomonari Kobayashi ◽  
Toshitsugu Tanaka ◽  
Toshihiro Kawaguchi ◽  
Tetsuichiro Mukai ◽  
Yutaka Tsuji

Author(s):  
Behrad Esgandari ◽  
Shahab Golshan ◽  
Reza Zarghami ◽  
Rahmat Sotudeh‐Gharebagh ◽  
Jamal Chaouki

2019 ◽  
Vol 9 (3) ◽  
pp. 572 ◽  
Author(s):  
Syed Ali ◽  
Avijit Basu ◽  
Sulaiman Alfadul ◽  
Mohammad Asif

In the present study, we report the fluidization behavior of ultrafine nanopowder using the assisted fluidization technique of particle mixing, which was further superimposed with the pulsation of the inlet gas flow to the fluidized bed. The powder selected in the present study was hydrophilic nanosilica, which shows strong agglomeration behavior leading to poor fluidization hydrodynamics. For particle mixing, small proportions of inert particles of Geldart group A classification were used. The inlet gas flow to the fluidized bed was pulsed with a square wave of frequency 0.1 Hz with the help of a solenoid valve controlled using the data acquisition system (DAQ). In addition to the gas flow rate to the fluidized bed, pressure transients were carefully monitored using sensitive pressure transducers connected to the DAQ. Our results indicate a substantial reduction in the effective agglomerate size as a result of the simultaneous implementation of the assisted fluidization techniques of particle mixing and flow pulsation.


1999 ◽  
Vol 175 (1) ◽  
pp. 117-130 ◽  
Author(s):  
T. DYAKOWSKI ◽  
S. J. WANG ◽  
D. GELDART ◽  
M. S. BECK

1964 ◽  
Vol 19 (12) ◽  
pp. 1001-1002 ◽  
Author(s):  
D.H. Glass ◽  
D. Harrison
Keyword(s):  

2011 ◽  
Vol 354-355 ◽  
pp. 338-343
Author(s):  
Qian Jun Li ◽  
Dong Ping Zhang

Experimental investigations on hydrodynamic characteristics of cylindrical pressurized spout-fluidizing bed were carried out. Two kinds of millet were used as bed materials. The operational pressure is 0.1MPa~0.4MPa (absolutely pressure). Five distinct flow patterns, i.e, fixed bed(FB), jet in fluidized bed with bubbles(JFB), jet in fluidized bed with slugging(JFS), spout with aeration(SA) and spout-fluidizing bed(SF) were identified. Effects of the static bed height and operational pressure on the flow pattern map were particularly studied. Typical flow pattern images obtained by a high- resolution digital CCD camera were presented for classifying these flow patterns. Typical flow pattern maps were plotted for describing the transitions between flow patterns with operating conditions


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