[1] Liu Y, Li G H, Sirpa K. Hydrodynamic modeling of dense gas-particle turbulence flows under microgravityspace environments [J]. Microgravity Science and Technology, 2011, 23(1): 1-11.[2] Zhou L X. Second-order moment modeling of dispersed two-phase turbulence. Part 2. USM-θ two-phase turbulence model and USM-SGS two-phase stressmodel [J]. Science China Physics, Mechanics & Astronomy,2011, 54(7): 1296-1303.[3] Xiang J S, Mcglinchey D, Latham J P. An investigation of segregation and mixing in dense phase pneumatic conveying [J]. Granular Matter, 2010, 12(4):345-355.[4] Wang Q C, Zhang K, Gu H Y. CFD simulation of pressure fluctuation characteristics in the gassolidfluidized bed: Comparisons with experiments [J].Petroleum Science, 2011, 8(2): 211-218.[5] Cheng Y, Guo Y C, Wei F, et al. Modeling the hydrodynamics of downer reactors based on kinetic theory[J]. Chemical Engineering Science, 1999, 54(13-14): 2019-2027.[6] Zheng Y, Wan X T, Qian Z, et al. Numerical simulation of the gas-particle turbulent flow in riser reactorbased on k-ε-kp-εp-θ two-fluid model [J]. Chemical Engineering Science, 2001, 56(24): 6813-6822.[7] Yu Y, Zhou L X, Wang B G, et al. A USM-θ two-phase turbulence model for simulating dense gasparticleflows [J]. Acta Mechanica Sinica, 2005, 21(2):228-234.[8] Zeng Z X, Zhou L X, Zhang J. A two-scale secondorder moment two-phase turbulence model for simulatingdense gas-particle flows [J]. Acta Mechanica Sinica,2005, 21(5): 430-435.[9] Zhou Li-xing. Dynamics of multiphase turbulent reacting fluid flows [M]. Beijing: National Defense Industry Press, 2002 (in Chinese).[10] Gidaspow D. Multiphase flow and fluidization: Continuum and kinetic theory descriptions [M]. New York:Academic Press, 1994.[11] Horio M, Morishita K, Tachibana O, et al. Solid distribution and movement in circulating fluidizedbeds [C]// International Conference Proceedings of Circulating Fluidized Bed Technology II. Oxford: Pergamon Press, 1988.[12] Wang Z, Bai D, Jin Y. Hydrodynamics of cocurrent down flow circulating fluidized bed (CDCFB) [J]. Powder Technology, 1992, 70(3): 271-275. |