[1] Jensen,V.G.,"Viscous flow around a sphere at low Reynolds number (< 40)",Proc.R.Soc.Ser.A,249(1256),346-366 (1959). [2] Rimon,Y.,Cheng,S.I.,"Numerical solution of a uni-form flow over a sphere at intermediate Reynolds numbers",Phys.Fluids,12 (5),949-959 (1969). [3] LeClair,B.P.,Hamielec,A.E.,Pruppacher,H.R.,"A nu-merical study of the drag on a sphere at low and interme-diate Reynolds numbers",J.Atmos.Sci.,27 (3),308-315(1970). [4] Ryskin,G.,Leal,L.G.,"Numerical solution of free-boundary problems in fluid mechanics.Part 1.The finite-difference technique",J.Fluid Mech.,148,1-17 (1984). [5] Dandy,D.S.,Leal,L.G.,"Buoyancy-driven motion of adeformable drop through a quiescent liquid at intermediateReynolds numbers",J.Fluid Mech.208 161-192 (1989). [6] Mao,Z.Sh.,Chen,J.Y.,"Numerical solution of viscousflow past a solid sphere with the control volume formula-tion’’,Chinese J.Chem.Eng.,5 (2),105-116 (1997). [7] Li.T.W.,Sun,C.G.,Mao,Z.Sh.,Chen,J.Y.,"Influenceof distortion function on the accuracy of numerical simula-tion of the motion of a single buoyancy-driven deformabledrop",Huagong Yejin,20 (1),29-37 (1999).(in Chinese)also in Sel.Pap.Eng.Chem.Metall.(China) 1999,Xie,Y.S.,Mao,Z.Sh.,Xia,G.,eds.,Science Press,Beijing,92-102 (2000).(in English) [8] Mao,Z.S.,Li,T.W.,Chen,J.Y.,"Numerical simulationof steady and transient mass transfer to a single drop dom-inated by external resistance",Int.J.Heat Mass Transfer,44 (6),1235- 1247 (2001). [9] Li,T.W.,Mao,Z.Sh.,Chen J.Y.,Fei,W.Y.,"Experimen-tal and numerical investigations of single drop mass trans-fer in solvent extraction systems with resistance in bothphases",Chinese J.Chem.Eng.,10(1),1-14 (2002). [10] Hu,H.H.,"Direct simulation of flows of solid-liquid mix-tures’’,Int.J.Multiphase Flow,22 (2),335-352 (1996). [11] Zinchenko,A.Z.,Davis,R.H.,"An efficient algorithm forhydrodynamical interaction of many deformable drops",J.Comput.Phys.,157 (2),539-587 (2000). [12] Happel,J.,"Viscous flow in multiparticle systems: Slowmotion of fluids relative to beds of spherical particles",AIChE J.,4 (2),197-201 (1958). [13] LeClair,B.P.,Hamielec,A.E.,"Viscous flow throughparticle assemblages at intermediate Reynolds numbers-A cell model for transport in bubbles svarms",Can.J.Eng.Chem.,49 (6),713- 720 (1971). [14] Happel,J.,Brenner,H.,Low Reynolds Number Hydrody-namics,2nd,Noordhoff,Leydon the Netherlands (1973). [15] El-Kaissy,M.M.,Homsy,G.M.,"A theoretical study ofpressure drop and transport in packed beds at intermediateReynolds numbers",Ind.Eng.Chem.Fundam.,12 (1),82-90 (1973). [16] Mohan,V.,Raguraman,J.,"A theoretical study of pressuredrop for non-Newtonian creeping flow past an assemblageof spheres",AIChE J.,22 (2),259-264 (1976). [17] Gu,D.Z.,Li,Z.X,Wu,D.C.,"Non-Newtonian flowthrough assemblage of uniform spheres",J.Chengdu Uni.Sci.Technol.,(4),1-12 (1992).(in Chinese) [18] Kuwabara,S.,"The forces experienced by randomly dis-tributed parallel cylinders or spheres in a viscous flow atsmall Reynolds numbers",J Phys.Soc.Japan,14 (4),527-532 (1959). [19] LeClair,B.P.,Hamielec,A.E.,"Viscous flow throughparticle assemblages at intermediate Reynolds numbers-Steady-state solutions for flow through assemblages ofspheres",Ind.Eng.Chem.Fundam.,7 (4),542-549(1968). [20] Tal(Thau),R.,Sirignano,W.A.,"Cylindrical cell model forthe hydrodynamics of particle assemblages at intermediateRynolds numbers",AIChE J.,28 (2),233-237 (1982). [21] Tal(Thau),R.,Lee,D.N.,Sirignano.W.A.,"Hy-drodynamics and heat transfer in sphere assemblages-Cylindrical cell model",Int.J.Heat Mass Transfer,26(9),1265-1273 (1983). [22] Ryskin,G.,Leal,L.G.,"Orthogonal mapping",J.Comput.Phys.,50 (1),71-100 (1983). [23] Clift,R.,Grace,J.R.,Weber,M.E.,Bubbles,Drops,andParticles,Academic Press,New York,112 (1978). [24] Barnea,E.,Mizrahi,J.,"A generalized approach to thefluid dynamics of particulate systems.part 1.General cor-relation for fluidization and sedimentation in solid multi- particle systems",Chem.Eng.J.,5 (2),171 189 (1973). [25] Yang,W.-C.,"30-years of industrial research on fluid-ization-Bridging the gap between theory and practice",in Fluidization IX,Fan,L.-S.,Knowlton,T.D.,eds.,Engi-neering Foundation,New York,31-43 (1998). [26] Khan,A.R.,Richardson,J.F.,"Pressure gradient and fric-tion factor for sedimentation of uniform spheres in liquids",Chem.Eng.Sci.,45 (1),255 265 (1990). [27] Loeffier,A.L.Jr.,Ruth,B.F.,"Particulate fluidizationand sedimentation of spheres",AIChE J.,5 (3),310-314(1959). |