Articles & Issues
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received February 1, 2011
Accepted April 5, 2011
- 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.
Copyright © KIChE. All rights reserved.
All issues
Type transition in onset condition of turbulent fluidization
Department of Chemical Engineering, Konkuk University, Seoul 143-701, Korea 1Korea Institute of Energy Research, Daejon 305-343, Korea
choijhoo@konkuk.ac.kr
Korean Journal of Chemical Engineering, October 2011, 28(10), 2009-2011(3), 10.1007/s11814-011-0091-8
Download PDF
Abstract
The type transition in onset condition of turbulent fluidization in gas fluidized beds was investigated to obtain the relation representing more precise roles of physical properties of gas and solid particles. The type transition in onset condition of turbulent fluidization occurs at Archimedes number of 20.87 by type transition of bubble breakup. The maximum stable bubble diameter (dbmax) is greater than the equilibrium bubble diameter (dbeq) in the region, Ar<_x000D_
20.87, but dbeq>dbmax in the region, Ar>20.87. Therefore, the onset of turbulent fluidization is determined in the region, Ar<20.87, by dbeq and in the region, Ar>20.87, by dbmax as the limit of bubble growth. The uc decreases in the region, Ar<20.87, but increases in the region, Ar>20.87 as temperature increases.
References
Harrison D, Davidson JF, de Kock JW, Trans. Inst. Chem. Eng., 39, 202 (1961)
Morooka S, Tajima K, Miyauchi T, Int. Chem. Eng., 12, 168 (1972)
Werther J, In Fluidization Technology, Keairns DL Eds., Hemisphere, 215 (1976)
Werther J, In Fluidization IV, Kunii D, Toei R Eds., Engineering Foundation, New York, 93 (1984)
Chehbouni A, Chaouki J, Guy C, Klvana D, in Fluidization VIII, Large JF, Lagu’rie C Eds., Engineering Foundation, New York, 149 (1995)
Peeler PK, Lim KS, Close RC, in Circulating Fluidized Bed Technology VI, J. Werther Eds., DECHEMA, Frankfurt, Vol. 1, 125 (1999)
Choi JH, Ryu HJ, Yi CK, Korean J. Chem. Eng., 28(1), 304 (2011)
Wen CY, Yu YH, AIChE J., 12, 610 (1966)
Morooka S, Tajima K, Miyauchi T, Int. Chem. Eng., 12, 168 (1972)
Werther J, In Fluidization Technology, Keairns DL Eds., Hemisphere, 215 (1976)
Werther J, In Fluidization IV, Kunii D, Toei R Eds., Engineering Foundation, New York, 93 (1984)
Chehbouni A, Chaouki J, Guy C, Klvana D, in Fluidization VIII, Large JF, Lagu’rie C Eds., Engineering Foundation, New York, 149 (1995)
Peeler PK, Lim KS, Close RC, in Circulating Fluidized Bed Technology VI, J. Werther Eds., DECHEMA, Frankfurt, Vol. 1, 125 (1999)
Choi JH, Ryu HJ, Yi CK, Korean J. Chem. Eng., 28(1), 304 (2011)
Wen CY, Yu YH, AIChE J., 12, 610 (1966)