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[1]Acrivos, A. and E. Herbolzheimer (1979). "Enhanced sedimentation in settling tanks with inclined walls." Journal of Fluid Mechanics 92(03): 435-457.
[2]Andrews, M. and P. O''Rourke (1996). "The multiphase particle-in-cell (MP-PIC) method for dense particulate flows." International Journal of Multiphase Flow 22(2): 379-402.
[3]Auton, T., et al. (1988). "The force exerted on a body in inviscid unsteady non-uniform rotational flow." Journal of Fluid Mechanics 197: 241-257.
[4]Berryman, J. G. (1983). "Random close packing of hard spheres and disks." Physical Review A 27(2): 1053.
[5]Boycott, A. (1920). "Sedimentation of blood corpuscles." Nature 104(2621): 532-532.
[6]Chorin, A. J. (1967). "The numerical solution of the Navier-Stokes equations for an incompressible fluid." Bulletin of the American Mathematical Society 73(6): 928-931.
[7]Chou, Y.-J., et al. (2015). "An Euler–Lagrange model for simulating fine particle suspension in liquid flows." Journal of Computational Physics 299: 955-973.
[8]Chou, Y.-J. and Y.-C. Shao (2016). "Numerical study of particle-induced Rayleigh-Taylor instability: Effects of particle settling and entrainment." Physics of Fluids 28(4): 043302.
[9]Cui, A. (1999). On the parallel computation of turbulent rotating stratified flows, Stanford University.
[10]Cundall, P. A. and O. D. Strack (1979). "A discrete numerical model for granular assemblies." geotechnique 29(1): 47-65.
[11]Duran, J. and T. Mazozi (1999). "Granular boycott effect: How to mix granulates." Physical Review E 60(5): 6199.
[12]Gibilaro, L., et al. (1985). "Generalized friction factor and drag coefficient correlations for fluid-particle interactions." Chemical Engineering Science 40(10): 1817-1823.
[13]Gidaspow, D. (1994). Multiphase flow and fluidization: continuum and kinetic theory descriptions, Academic press.
[14]Graham, W. and R. Lama (1963). "Continuous thickening in an inclined thickener." The Canadian Journal of Chemical Engineering 41(4): 162-165.
[15]Herbolzheimer, E. (1983). "Stability of the flow during sedimentation in inclined channels." Physics of Fluids 26(8): 2043-2054.
[16]Herbolzheimer, E. and A. Acrivos (1981). "Enhanced sedimentation in narrow tilted channels." Journal of Fluid Mechanics 108: 485-499.
[17]Hill, W. D., et al. (1977). "Boundary-enhanced sedimentation due to settling convection." International Journal of Multiphase Flow 3(6): 561-583.
[18]Hoomans, B. P. B. (2000). Granular dynamics of gas-solid two-phase flows, Universiteit Twente.
[19]Hoomans, B. P. B., et al. (1996). "Discrete particle simulation of bubble and slug formation in a two-dimensional gas-fluidised bed: A hard-sphere approach." Chemical Engineering Science 51(01): 99-118.
[20]Kaushal, D., et al. (2012). "CFD modeling for pipeline flow of fine particles at high concentration." International Journal of Multiphase Flow 43: 85-100.
[21]Kinosita, K. (1949). "Sedimentation in tilted vessels (1)." Journal of Colloid Science 4(5): 525-536.
[22]Lundgren, R. (1927). "A study of the physical nature of the sedimentation of blood‐corpuscles." Journal of Internal Medicine 67(1): 63-104.
[23]Nakamura, H. and K. Kuroda (1937). "La cause de l’acceleration de la vitesse de sedimentation des suspensions dans les recipients inclines." Keijo J. Med 8: 256-296.
[24]Patankar, N. and D. Joseph (2001). "Lagrangian numerical simulation of particulate flows." International Journal of Multiphase Flow 27(10): 1685-1706.
[25]Patankar, N. and D. Joseph (2001). "Modeling and numerical simulation of particulate flows by the Eulerian–Lagrangian approach." International Journal of Multiphase Flow 27(10): 1659-1684.
[26]Pearce, K. (1962). Settling in the presence of downward-facing surfaces. Proceedings of the Symposium on the Interaction between Fluids and Particles, London.
[27]Ponder, E. (1925). "On sedimentation and rouleaux formation." Experimental Physiology 15(3): 235-252.
[28]Richardson, J. and W. Zaki (1954). "The sedimentation of a suspension of uniform spheres under conditions of viscous flow." Chemical Engineering Science 3(2): 65-73.
[29]Snider, D., et al. (1998). "Sediment flow in inclined vessels calculated using a multiphase particle-in-cell model for dense particle flows." International Journal of Multiphase Flow 24(8): 1359-1382.
[30]van der Hoef, M. A., et al. (2006). "Multiscale modeling of gas-fluidized beds." Advances in chemical engineering 31: 65-149.
[31]Vohra, D. and B. Ghosh (1971). "Studies of sedimentation in inclined tubes." Indust. Engng Chem 13: 3240.
[32]Xu, Z.-J. and E. E. Michaelides (2005). "A numerical simulation of the Boycott effect." Chem. Eng. Comm. 192(4): 532-549.
[33]Zahavi, E. and E. Rubin (1975). "Settling of solid suspensions under and between inclined surfaces." Industrial & Engineering Chemistry Process Design and Development 14(1): 34-41.
[34]Zhang, D. and A. Prosperetti (1997). "Momentum and energy equations for disperse two-phase flows and their closure for dilute suspensions." International Journal of Multiphase Flow 23(3): 425-453.
[35]古詩弘 (2014). "固液二相懸浮微粒問題之雙向耦合數值模式." 臺灣大學應用力學研究所學位論文.
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