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Received July 26, 2004
Accepted October 11, 2004
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Influence of Hydrodynamic Parameters on Particle Attrition during Fluidization at High Temperature
Department of Environmental Engineering, National Chung-Hsing University, Taichung, 402, Taiwan
Korean Journal of Chemical Engineering, January 2005, 22(1), 154-160(7), 10.1007/BF02701478
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Abstract
In a fluidized bed, attrition both increases the number of particles and reduces particle size, which may affect reactor performance, fluidizing properties, operating stability and operating costs. Most fluidized applications are conducted at high temperature, but in the past most attrition correlations were performed at room temperature, so the attrition rate at high temperature could not be predicted. In contrast, this study investigates the attrition rate of fluidized materials at high temperature. Silica sand was used as the bed material; the operating parameters included temperature, particle size, static bed height and gas velocity to assess the attrition rate. Then an appropriate correlation was developed by regression analysis to predict attrition rate at high temperature. Experimental results indicated that the attrition rate increases with increasing temperature. In addition, the particle attrition increased as average particle size decreased because the probability of collision increases with surface area. The attrition rate increased with increasing gas velocity because of increased kinetic stress of particle movement. The actual density and viscosity of air at specific fluidization temperature were modified and an Ar number was introduced to fit our experimental data. The experimental correction agrees with the experimental results, which can predict particle attrition rate at high temperatures.
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Kono H, AIChE Symp. Ser., 77, 96 (1981)
Lee CG, Kim JS, Song PS, Choi GS, Kang Y, Choi MJ, Korean J. Chem. Eng., 20(1), 133 (2003)
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Lee WJ, Kim SD, Song BH, Korean J. Chem. Eng., 19(6), 1091 (2002)
Lim TH, Kim SD, Korean J. Chem. Eng., 21(4), 905 (2004)
Lin CL, Wey MY, Korean J. Chem. Eng., 20(6), 1123 (2003)
Lin CL, Wey MY, You SD, Powder Technol., 126(3), 297 (2002)
Lin L, Sesrs JT, Wen CY, Powder Technol., 27, 105 (1980)
Merrick D, Highley J, AIChE Symp. Ser., 70, 366 (1974)
Na YS, Kim DH, Lee CH, Lee SW, Park YS, Oh YK, Park SH, Song SK, Korean J. Chem. Eng., 21(2), 430 (2004)
Park YS, Kim HS, Shun D, Song KS, Kang SK, Korean J. Chem. Eng., 17(3), 284 (2000)
Ray YC, Jiang TS, Powder Technol., 49, 193 (1987)
Svoboda K, Hartman M, Ind. Eng. Chem. Process Des. Dev., 20, 319 (1981)
Ulerich NH, Vaux RA, Newby RA, Keairns DL, Experimental/Engineering Support for EPAs PBC Program, Final Rep., EPA-600/7-80-015A, Westinghouse Research and Development Center, Pittsburgh, PA, USA, Jan. (1980)
Vaux WG, Fellers AW, AIChE Symp. Ser., 77, 107 (1981)
Vaux WG, Schruben JS, AIChE J., 79, 97 (1978)
Wu SY, Baeyens J, Powder Technol., 67, 217 (1991)
Wu SY, Chu CY, "Attrition in a Gas Fluidized Bed with Single High Velocities Vertical Nozzle", World Congress on Particle Technology 3rd, Brighton, U.K., 152 (1998)
Wu SY, Baeyens J, Chu CY, Can. J. Chem. Eng., 77(4), 738 (1999)