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Received January 26, 2009
Accepted March 5, 2009
- 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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CFD simulation of gas-solid bubbling fluidized bed containing FCC particles
Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan 98164-161, Iran
hosseini@mail.usb.ac.ir
Korean Journal of Chemical Engineering, September 2009, 26(5), 1405-1413(9), 10.1007/s11814-009-0220-9
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Abstract
The hydrodynamics of a bubbling gas-solid fluidized bed of 57.4 μm FCC particles was simulated by using a state-of-the-art two-fluid model integrating the kinetic theory of granular flow for particulate phase stresses. The overestimation of the bed expansion was resolved by using a suitable scale factor in the drag model as suggested by McKeen and Pugsley (T.R. McKeen, T.S. Pugsley, Powder Technol., 129, 139 (2003)). This study showed that the method was_x000D_
appropriate in simulation of a gas-solid fluidized bed of Geldart A particles at high gas velocities (0.3 to 0.61 m/s). The reduction of computational time especially for simulation of large-scale systems was achieved. The time-averaged local voidage was compared with the experimental data and the trend of varying several parameters on the hydrodynamic of the bed was investigated. The simulation results showed both qualitative and quantitative agreement with the literature.
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References
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McKeen T, Pugsley T, Powder Technol., 129(1-3), 139 (2003)
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Syamlal M, O’Brien TJ, Office of fossil energy, national energy technology laboratory, Morgantown, WV, April (1987)
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Gibilaro LG, Di Felice R, Waldram SP, Chem. Eng. Sci., 40, 1817 (1985)
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Ellis N, Ph.D. Thesis, University of British Columbia, Vancouver, British Columbia, Canada (2003)
Yongmin Z, Chunxi L, 3rd Asian Particle Technol. Symp., 392 (2007)
Pain CC, Mansoorzadeh S, de Oliveira CRE, Int. J. Multiph. Flow, 27(3), 527 (2001)
Zhu H, Zhu J, Li G, Li F, Powder Technol., 180, 339 (2008)
Chalermsinsuwan B, Kuchonthara P, Piumsomboon P, Chem. Eng. Process., 48, 165 (2009)
Zhong W, Zhang Y, Jin B, Zhang M, Chem. Eng. Technol., 32, 1 (2009)
Danilov V, Lim J, Moon I, Choi KH, Korean J. Chem. Eng., 23(5), 753 (2006)
Park Y, Yun CY, Yi J, Kim H, Korean J. Chem. Eng., 22(5), 697 (2005)
Ranade, VV, Computational flow modeling for chemical reactor engineering, 1st, ed., Academic Press (2002)
Chiesa M, Mathiesen V, Melheim JA, Halvorsen B, Comput. Chem. Eng., 29(2), 291 (2005)
van der Hoef MA, Annaland MV, Kuipers JAM, Chem. Eng. Sci., 59(22-23), 5157 (2004)
Jenkins JT, Savage SB, J. Fluid Mech., 30, 187 (1983)
Lun CKK, Savage SB, Jeffrey DJ, Chepurniy N, J. Fluid Mech., 140, 223 (1984)
van Wachem BGM, Schouten JC, Krishna R, van den Bleek CM, Chem. Eng. Sci., 54(13-14), 2141 (1999)
Ding J, Gidaspow D, AIChE J., 36, 523 (1990)
Pain CC, Mansoorzadeh S, de Oliveira CRE, Goddard AJH, Int. J. Multiph. Flow, 36, 91 (2001)
van Wachem BGM, Schouter JC, Krishna R, van den Bleek CM, Comput. Chem. Eng., 22, S299 (1998)
Patil DJ, Annaland AV, Kuipers JAM, Chem. Eng. Sci., 60(1), 73 (2005)
Massimilla L, Donsi G, Powder Technol., 15, 253 (1976)
Grace JR, Sun G, Can. J. Chem. Eng., 69, 1126 (1991)
Ferschneider G, Mege P, Rev. Inst. Fr. Pet., 51(2), 301 (1996)
Bayle J, Mege P, Gauthier T, In: Kwauk M, Li J, Yang WC (Eds.), Fluidization X, Engineering Foundation, New York, p. 125 (2001)
Patureaux T, Barthod D, Oil Gas Sci. Technol.-Rev. IFP, 55, 219 (2000)
Krishna R, van Baten JM, Chem. Eng. J., 82(1-3), 247 (2001)
Seukim H, Arastoopour H, Can. J. Chem. Eng., 73(5), 603 (1995)
Kim H, Arastoopour H, Powder Technol., 122(1), 83 (2002)
McKeen T, Pugsley T, Powder Technol., 129(1-3), 139 (2003)
Zimmermann S, Taghipour F, Ind. Eng. Chem. Res., 44, 918 (2005)
Syamlal M, O’Brien TJ, Office of fossil energy, national energy technology laboratory, Morgantown, WV, April (1987)
Li T, Pougatch K, Salcudean M, Grecov D, Powder Technol., 184, 89 (2008)
Ye M, Wang J, van der Hoef MA, Kuipers JAM, Particuology, 6, 540 (2008)
Ye M, Ph.D. Thesis, University of Twente, Enschede, Netherlands (2005)
Wang J, vander Hoef MA, Kuipers JAM, Chem. Eng. Sci., 64, 622 (2009)
Gibilaro LG, Di Felice R, Waldram SP, Chem. Eng. Sci., 40, 1817 (1985)
Fluent 6.3, User’s Guide, 23.5 Eulerian Model, Fluent Inc. (2006)
Patil DJ, Annaland MV, Kuipers JAM, Chem. Eng. Sci., 60(1), 57 (2005)
Lu HL, He YR, Liu WT, Ding JM, Gidaspow D, Bouillard J, Chem. Eng. Sci., 59(4), 865 (2004)
Du W, Bao XJ, Xu J, Wei WS, Chem. Eng. Sci., 61(14), 4558 (2006)
Taghipour F, Ellis N, Wong C, Chem. Eng. Sci., 60(24), 6857 (2005)
van Wachem BGM, Schouten JC, van den Bleek CM, Krishna R, Sinclair JL, AIChE J., 47(5), 1035 (2001)
Ahuja GN, Patwardhan W, DOI:10.1016/j.cej.2008.03.011.
Patil DJ, Smit J, van Sint Annaland M, Kuipers JAM, AIChE J., 52, 58 (2007)
Ma D, Ahmadi G, J. Chem. Phys., 84, 3449 (1986)
Lettieri P, Micale G, Cammarata L, Colman D, in Proc. 10th Workshop on Two-Phase Flow Predictions, Merseburg, 300 (2002)
Cammarata L, Lettieri P, Micale GDM, Colman D, Int. J. Chem. Reactor Eng., 1, A3 (2003)
Ellis N, Ph.D. Thesis, University of British Columbia, Vancouver, British Columbia, Canada (2003)
Yongmin Z, Chunxi L, 3rd Asian Particle Technol. Symp., 392 (2007)
Pain CC, Mansoorzadeh S, de Oliveira CRE, Int. J. Multiph. Flow, 27(3), 527 (2001)
Zhu H, Zhu J, Li G, Li F, Powder Technol., 180, 339 (2008)