Abstract
Numerical simulations based on the Eulerian-Eulerian approach have been performed in the study of interphase heat transfer in a gas solid fluidized bed. The kinetic theory of granular flow (KTGF) has been used to describe the solid phase rheology. An assessment of drag models in the prediction of heat transfer coefficients shows that no major difference is observed in the choice of the drag model used. Fluctuations of the interphase heat transfer coefficient have been found to be closely related to the bubble motion in the bed. Effects of the wall boundary condition, inlet gas velocity, initial bed height and particle size on the predicted heat transfer coefficient have also been investigated. Typical temperature profiles in the bed show that thermal saturation is attained instantaneously close to the gas distributor. Simulated results of the coefficients are in fair agreement with those reported in literature.
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Refrerences
H. S. Mickley and D. F. Fairbanks, AIChE J., 1, 374 (1955).
R. S. Brodkey, D. S. Kim and W. Sidner, Int. J. Heat Mass Transfer, 34, 2327 (1991).
R. S. Figliola and D. E. Beasley, Chem. Eng. Sci., 48, 2901 (1993).
R. Yusuf, B. Halvorsen and M.C. Melaaen, Int. J. Multiphase Flow, 42, 9 (2012).
J. Kuipers, W. Prins and W. Swaaij, AIChE J., 38, 1079 (1992).
M. Syamlal and D. Gidaspow, AIChE J., 31, 127 (1985).
D. Patil, J. Smit, M. Sint Annaland and J. Kuipers, AIChE J., 52, 58 (2006).
L. Armstrong, S. Gu and K. Luo, Int. J. Heat Mass Transfer, 53, 4949 (2010).
C. Delvosalle and J. Vanderschuren, Chem. Eng. Sci., 40, 769 (1985).
J. Chang, G. Wang, J. Gao, K. Zhang, H. Chen and Y. Yang, Powder Technol., 217, 50 (2012).
Y. Yang, J. Yang, W. Chen and S. Rong, Ind. Eng. Chem. Res., 41, 2579 (2002).
D. Kunii and O. Levenspiel, Fluidization engineering, Butterworth-Heinemann Boston (1991).
Y. Kaneko, T. Shiojima and M. Horio, Chem. Eng. Sci., 54, 5809 (1999).
Y. Behjat, S. Shahhosseini and S. H. Hashemabadi, International Communications in Heat and Mass Transfer, 35, 357 (2008).
M. Hamzehei, H. Rahimzadeh and G. Ahmadi, Ind. Eng. Chem. Res., 49, 5110 (2010).
X. Z. Chen, Z.H. Luo, W. C. Yan, Y. H. Lu and I. S. Ng, AIChE J., 57, 3351 (2011).
M. Syamlal and T. J. O’Brien, AIChE Symposium Series, 85, 22 (1989).
M. Syamlal and T. J. O’Brien, The derivation of a drag coefficient formula from velocity-voidage correlations, US Department of Energy, Morgantown (1987).
D. Gidaspow, Multiphase flow and fluidization: Continuum and kinetic theory descriptions, Academic Press (1994).
J. Cao and G. Ahmadi, Int. J. Multiphase Flow, 21, 1203 (1995).
S. Benyahia, M. Syamlal and T. J. O’Brien, Powder Technol., 162, 166 (2006).
C. Lun, S. Savage, D. Jeffrey and N. Chepurniy, J. Fluid Mech., 140, 223 (1984).
D.G. Schaeffer, Journal of Differential Equations, 66, 19 (1987).
D. Ma and G. Ahmadi, J. Chem. Phys., 84, 3449 (1986).
D. Gunn, Int. J. Heat Mass Transfer, 21, 467 (1978).
W. Ranz and W. Marshall, Chem. Eng. Prog., 48, 141 (1952).
N. Wakao, S. Kaguei and T. Funazkri, Chem. Eng. Sci., 34, 325 (1979).
A. Cybulski, M. J. Van Dalen, J.W. Verkerk and P. J. Van Den Berg, Chem. Eng. Sci., 30, 1015 (1975).
P. A. Nelson and T. R. Galloway, Chem. Eng. Sci., 30, 1 (1975).
B. Bird, W. Stewart and E. Lightfoot, Transport phenomena, revised 2nd Ed., John Wiley & Sons, Inc. (2006).
N.G. Deen, S. H. L. Kriebitzsch, M. A. Van der Hoef and J. A. M. Kuipers, Chem. Eng. Sci., 81, 329 (2012).
J. Sun, Y. Zhou, C. Ren, J. Wang and Y. Yang, Chem. Eng. Sci., 66, 4972 (2011).
F. Taghipour, N. Ellis and C. Wong, Chem. Eng. Sci., 60, 6857 (2005).
P. Johnson and R. Jackson, J. Fluid Mech., 176, 67 (1987).
T. Li, J. Grace and X. Bi, Powder Technol., 203, 447 (2010).
R. Yusuf, M. C. Melaaen and V. Mathiesen, Chem. Eng. Technol., 28, 13 (2005).
S. Cloete, S. T. Johansen and S. Amini, Powder Technol., 239, 21 (2013).
C. Loha, H. Chattopadhyay and P. K. Chatterjee, Chem. Eng. Sci., 75, 400 (2012).
F. Vejahati, N. Mahinpey, N. Ellis and M. B. Nikoo, Can. J. Chem. Eng., 87, 19 (2009).
L.M. Armstrong, S. Gu and K. H. Luo, Int. J. Multiphase Flow, 36, 916 (2010).
J. R. Grace, Powder Technol., 113, 242 (2000).
J. S. M. Botterill, Fluid-bed heat transfer: Gas-fluidized bed behaviour and its influence on bed thermal properties, Academic Press, London (1975).
C. Loha, H. Chattopadhyay and P. K. Chatterjee, Particuology, 11, 673 (2013).
J. Tuot and R. Clift, AIChE Symp. Ser., 78 (1973).
O.-a. Jaiboon, B. Chalermsinsuwan, L. Mekasut and P. Piumsomboon, Powder Technol., 233, 215 (2013).
A. P. Baskakov, V.G. Tuponogov and N. F. Filippovsky, Powder Technol., 45, 113 (1986).
O. Olaofe, M. Van der Hoef and J. Kuipers, Chem. Eng. Sci., 66, 2764 (2011).
X. Z. Chen, D. P. Shi, X. Gao and Z. H. Luo, Powder Technol., 205, 276 (2011).
J. Wang, C. Ren, Y. Yang and L. Hou, Ind. Eng. Chem. Res., 48, 8508 (2009).
S. Cloete, S. T. Johansen and S. Amini, Powder Technol., 239, 21 (2013).
M. L. DeChellis, J.R. Griffin and M. E. Muhle, US Patent, 5, 405, 922 (1995).
C. Van Heerden, A. Nobel and D. Van Krevelen, Ind. Eng. Chem., 45, 1237 (1953).
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Lungu, M., Sun, J., Wang, J. et al. Computational fluid dynamics simulations of interphase heat transfer in a bubbling fluidized bed. Korean J. Chem. Eng. 31, 1148–1161 (2014). https://doi.org/10.1007/s11814-014-0022-6
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DOI: https://doi.org/10.1007/s11814-014-0022-6