[1] Li, Y., Kwauk, M., "The dynamics of fast fluidization", Fluidization, Grace, J.R.,
Matsen, J.M., Eds., Plenum Press,New York, 537-544 (1980).
[2] Kuipers, J.A.M., van Duin, K.J., van Beckum, F.P.H., van Swaaij, W.P.M., "A numerical
model of gas-fluidized beds", Chem. Eng. Sci., 47 (8), 1913-1924 (1992).
[3] Gidaspow, D., Multiphase Flow and Fluidization: Continuum and Kinetic Theory
Description, Academic Press, Boston (1994).
[4] Neri, A., Gidaspow, D., "Riser hydrodynamics: Simulationusing kinetic theory", AIChE
J., 46 (1), 52-67 (2000).
[5] Sundaresan, S., "Modeling the hydrodynamics of multi phase flow reactors: current
status and challenges", AIChEJ., 46 (6), 1102-1105 (2000).
[6] Wang, W., Li, Y., "Hydrodynamic simulation of fluidization by using a modified kinetic
theory", Ind. Eng. Chem. Res., 40 (23), 5066-5073 (2001). .
[7] Wang, W., Li, Y., "Pseudo-fluid simulation of transient behaviors in a CFB riser",
Chinese J. Chem. Eng., 10 (1),77-83 (2002).
[8] Hommans, B.P.B., Kuipers, J.A.M., Briels, W.J., van Swaaij, W.P.M., "Discrete particle
simulation of bubbles and slug formation in a two-dimensional gas-fluidized bed: a hard-
sphere approach", Chem. Eng. Sci., 51 (1), 99-108 (1996).
[9] Xu, B.H., Yu, A.B., "Numerical simulation of the gas solid flow in a fluidized bed by
combining discrete particle method with computational fluid dynamics", Chem. Eng.Sci., 52
(16), 2785-2809 (1997).
[10] Ouyang, J., Li, J., "Discrete simulation of heterogeneous structure and dynamic
behavioir in gas-solid fluidization", Chem. Eng. Sci., 54 (22), 5427-5440 (1999).
[11] Li, J., Kwauk, M., Particle-fluid Two-phase Flow-The Energy-Minimization Multi-scale
Model, Metallurgy Industry Press, Beijing (1994).
[12] Wang, L., Zhang, L., Jin, D., Li, J., "Experimental study on gas-solid mass transfer
in circulating fluidized beds", Chi nese J. Chem. Eng., 10 (1), 70-76 (2002).
[13] Wen, C.Y., Yu, Y.H., "Mechanics of fluidization", Chem. Eng. Pro. Symp. Ser, 62, 100-
111 (1966).
[14] Ergun, S., "Fluid flow through packed columns", Chem. Eng. Progr., 48 (2), 89-91
(1952).
[15] Gunn, D.J., Malik, A.A., "The structure offluidized beds in particulate fluidization",
Proceedings of the International Symposium on Fluidization, Dringkenburg, A.A.,
Ed.,Netherlands University Press, Eindhoven, 52-65 (1967).
[16] Mueller, P., Reh, L., "Particle drag and pressure drop in a accelerated gas-solid
flow", CFB-IV, Avidan, A.A., Ed.,AIChE, New York, 159-166 (1994).
[17] Huang, W., Zhu, J., "An experimental investigation on solid acceleration length in the
riser of a long circulating fluidized bed", Chinese J. Chem. Eng., 9 (1), 70-76 (2001).
[18] Li, Y., Chen, B., Wang, F., Wang, Y., "Hydrodynamic correlations for fast
fludization", Fluidization: Science and Technology, Science Press, Beijing, 124-133 (1982).
[19] Bai, D.R., Jin, Y., Yu, Z., "Acceleration of particles and momentum exchange between
gas and solids in fast fluidized beds", Fluidization: Science and Technology, Kwauk, M.,
Kunni, D., Eds., Science Press, Beijing, 46-55 (1991).
[20] Li, J., Wen, L., Ge, W., Cui, H., Ren, J., "Dissipative struc ture in concurrent-up
gas-solid flow", Chem. Eng. Sci., 53 (19), 3367-3379 (1998).
[21] Li, J., Cheng, C., Zhang, Z., Yuan, J., Nemet, A., Fett, F.N., "The EMMS model-its
application, development and updated concepts", Chem. Eng. Sci., 54 (22), 5409- 5425
(1999).
[22] Li, J., "Compromise and resolution-Exploring the multi- scale nature of gas-solid
fiuidization", Powder Technol., 111 (1-2), 50-59 (2000). |
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