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In relation to this article, we declare that there is no conflict of interest.
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Received March 14, 2010
Accepted May 29, 2010
articles 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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A model for the temperature effect on onset velocity of turbulent fluidization of Geldart type A particles

Department of Chemical Engineering, Konkuk University, Seoul 143-701, Korea 1Korea Institute of Energy Research, Daejeon 305-343, Korea
choijhoo@konkuk.ac.kr
Korean Journal of Chemical Engineering, January 2011, 28(1), 304-307(4), 10.1007/s11814-010-0337-x
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Abstract

This study proposes a model to predict the temperature effect on the onset velocity of turbulent fluidization (u(c)) of Geldart type A particles. It was found that void splitting could occur in the whole bed when the initial bubble size at the distributor (d(bo)) was greater than the maximum stable bubble size (d(bmax)) or the equilibrium bubble size (d(beq)). The proposed model was successful to fit the trend of temperature effect on the uc. When the bubble growth was limited_x000D_ by the d(bmax), the u(c) increased with an increase of temperature. However, when the d(beq) was smaller than d(bmax), the u(c) decreased with an increase of temperature because the minimum fluidizing velocity and thus the d(beq) decreased. The u(c) increased initially and decreased later when the d(beq)/d(bmax) starting with the ratio >1 decreased to the ratio <1 as temperature increased. The present model predicted the trend properly that any other existing correlations could not be able to reflect.

References

Bi HT, Ellis N, Abba IA, Grace JR, Chem. Eng. Sci., 55(21), 4789 (2000)
Chehbouni A, Chaouki J, Guy C and Klvana D, “Fluidization VIII” Edited by Large JF and Lagu’rie C, Engineering Foundation, New York, 149 (1995)
Peeler PK, Lim KS and Close RC, “Circulating Fluidized Bed Technology VI,” Edited by Werther J, 1, 125 (1999)
Cai P, Chen SP, Jin Y, Yu ZQ, Wang ZW, AIChE Symposium Series., 85(270), 37 (1989)
Cai P, Jin Y, Yu ZQ, Fan LS, Ind. Eng. Chem, Res., 31, 632 (1992)
Harrison D, Davidson JF, de Kock JW, Trans. Instn. Chem.Eng., 39, 202 (1961)
Choi JH, Son JE, Kim SD, Ind. Eng. Chem. Res., 37(6), 2559 (1998)
Kunii D and Levenspiel O, Fluidization Engineering, 2nd Ed., Butterworth-Heinemann, Boston, 130 (1991)
Miwa K, Mori S, Kato T, Muchi I, Int. Chem. Eng., 12, 187 (1972)
Wen CY, Yu YH, AIChE J., 12, 610 (1966)

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