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Received January 12, 2014
Accepted April 16, 2014
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Entrainment of Geldart C particles in fluidized beds with binary particles
School of Chemical Engineering, Sungkyunkwan University, 2066 Seobu-ro, Jangan, Suwon 440-746, Korea 1Department of Chemical and Biomolecular Engineering and Energy & Environment Research Center, Korea Advanced Institute of Science and Technology, Daejeon 305-701, Korea 2Department of Chemical Engineering, Konkuk University, Seoul 143-701, Korea
dhlee@skku.edu
Korean Journal of Chemical Engineering, November 2014, 31(11), 2094-2100(7)
https://doi.org/10.1007/s11814-014-0113-4
https://doi.org/10.1007/s11814-014-0113-4
Abstract
The effects were determined of the mass ratio of Geldart C particles on the total amount of particles (Mfine/Mtotal=0-50 wt%), superficial gas velocity (Ug=0.5-1.0 m/s) and coarse particle size distribution (mono, binary, flat, and Gaussian type) on entrainment of Geldart C particles in a bubbling fluidized bed with binary particles (coarse particles:dp=0.512 mm, ρs=2,339 kg/m3 and Geldart C particles: dp=13 μm, ρs=4,455 kg/m3). The initial entrainment rate increases with increasing Ug. At Ug of 0.5 and 0.7 m/s, the initial entrainment rate slightly increases initially and then remains almost constant with increasing mass ratio (Mfine/Mtotal). At higher gas Ug of 0.85 and 1.0 m/s, the initial entrainment rate increases with increasing the mass ratio (Mfine/Mtotal) up to 30 wt%, after which the increasing slope of the initial entrainment rate decreases with increasing the mass ratio (Mfine/Mtotal). Also, the decrease in the coefficient of entrainment rate is equal to the increase in (Mfine/Mtotal) at the corresponding Ug. The average particle size of the entrained particles is about 12-16 μm at Ug of 0.5-1.0 m/s.
Keywords
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Ma XX, Honda Y, Nakagawa N, Kato K, J. Chem. Eng. Jpn., 29(2), 330 (1996)
Osberg GL, Charlesworth KH, Chem. Eng. Progress, 47, 566 (1951)
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Bachovchin DM, Beer JM, Sarofim AF, AIChE Symp. Ser., 205, 76 (1981)
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Sun G, Grace JR, AIChE J., 38, 716 (1992)
Rodriguez JM, Sanchez JR, Alvaro A, Florea DF, Estevez AM, Powder Technol., 111(3), 218 (2000)

