Author： SAADEVANDI BRAM
Publisher： Taylor & Francis Ltd
ISSN： 0098-6445
Source： Chemical Engineering Communications, Vol.191, Iss.10, 2004-10, pp. : 1379-1400
Disclaimer: Any content in publications that violate the sovereignty, the constitution or regulations of the PRC is not accepted or approved by CNPIEC.
Abstract
Particle motion in the spray region of a semicircular spouted-fluidized bed coating device was investigated. Radial and axial particle velocity and voidage profiles were obtained using computer-based video imaging techniques and custom software. In order to investigate the effect of liquid droplets on fluidized particles in the spray region, measurements were carried out both with and without an atomized water spray fed to the bed. In the draft tube region, radial profiles of particle velocities varied from parabolic to nearly flat. At the spray rates used in this work there was no difference in velocity and voidage measurements with or without spray.
Related content
Access to resources
Recommend
Estimating radial voidage profiles for all fluidization regimes in circulating fluidized bed risers
Powder Technology, Vol. 139, Iss. 2, 2004-01 ,pp. :
Growth kinetics in particle coating by top-spray fluidized bed systems
By Maronga Savini J. Wnukowski Piotr
Advanced Powder Technology, Vol. 12, Iss. 3, 2001-09 ,pp. :
Experimental study and particle population modeling of coating in a jet-fluidized bed
By Alavi S. M.
Advanced Powder Technology, Vol. 18, Iss. 3, 2007-04 ,pp. :
Particle flow model in a spouted bed
By Tsuji Toshiro Uemaki Osamu Itoh Hironori Shinohara Kunio
Advanced Powder Technology, Vol. 9, Iss. 2, 1998-01 ,pp. :