1 Sokolichin,A.,Eigenberger,G.,Lapin,A.,LÜbert,A.,“Dynamic numerical simulation of gas-liquid two-phase flows Euler/Euler versus Euler/Lagrange”,Chem.Eng.Sci.,52(4),611-62 2 Jakobsen,H.A.,Lindborg,H.,Dorao,C.A.,“Modeling of bubble column reactors,progress and limitations”,Ind.Eng.Chem.Res.,44 (14),5107-5151(2005). 3 Brackbill,J.U.,Kothe,D.B.,Zemach,C.,“A continuum method for modeling surface tension”,J.Comput.Phys.,100(2),335-354 (1992). 4 Clift,R.,Grace,J.R.,Weber,M.E.,Bubbles,Drops,and Particles, Academic Press,New York,30-33(1978). 5 Kwauk,M.S.,Li,H.Z.,Handbook of Fluidization,Chemical Industry Press,Beijing,106(2008).(in Chinese) 6 Tomiyama,A.,“Struggle with computational bubble dynamics”, Multiphase Sci.Technol.,10,369-405(1998). 7 Hu,S.,Kintner,R.C.,“The fall of single liquid drops through water”, AIChE J.,1(1),42-48(1955). 8 Brucato,A.,Grisafi,F.,Montante,G.,“Particle drag coefficients in turbulent fluids”,Chem.Eng.Sci.,53(18),3295-3314(1998). 9 Lane,G.L.,Schwarz,M.P.,Evans,G.M.,“Modeling of the interaction between gas and liquid in stirred vessels”,In:Proc.10th Eur. Conf.on Mixing,van den Akker,H.E.A.,Derksen,J.J.,eds.,Elsevier,Amsterdam,197-204(2000). 10 Khopkar,A.R.,Rammohan,A.R.,Ranade,V.V.,Dudukovic,M.P., “Gas-liquid flow generated by a Rushton turbine in stirred vessel: CARPT/CT measurements and CFD simulations”,Chem.Eng.Sci., 60(8/9),2215-2229(2005). 11 Blumberg,P.N.,Mohr,C.M.,“Effect of orientation on the settling characteristics of cylindrical particles”,AIChE J.,14(2),331-334 (1968). 12 Fan,L.,Mao,Z.S.,Yang,C.,“Experiment on sedimentation of slender particles with large aspect ratio and correlation of drag coefficient”,Ind.Eng.Chem.Res.,43(23),7664-7670Å2004). 13 Anderson,T.B.,Jackson,R.,“A fluid mechanical description of fluidized beds”,Ind.Eng.Chem.Fundam.,6(11),527-539(1967). 14 Homsy,G.M.,El-Kaissy,M.M.,Didwania,A.,“Instability waves and the origin of bubbles in fluidized beds-II”,Int.J.Multiphase Flow,6(4),305-318(1980). 15 Jakobsen,H.A.,Sanns,B.H.,Grevskott,S.,Svendsen,H.F.,“Modeling of vertical bubble-driven flows”,Ind.Eng.Chem.Res.,36(10), 4052-4074(1997). 16 Kuo,J.T.,Walls,G.B.,“Flow of bubbles through nozzles”,Int.J.Multiphase Flow,14(5),547-564(1988). 17 Sankaranarayanan,K.,Shan,X.,Kevrekidis,I.G.,Sundaresan,S., “Analysis of drag and virtual mass forces in bubbly suspensions using an implicit formulation of the lattice Boltzmann method”,J. Fluid Mech.,452,61-96(2002). 18 Kendoush,A.A.,Sulaymon,A.H.,Mohammed,S.A.M.,“Experimental evaluation of the virtual mass of two solid spheres accelerating in fluids”,Exp.Therm.Fluid Sci.,31(7),813-823(2007). 19 Odar,F.,“Verification of the proposed equation for calculation of the forces on a sphere accelerating in a viscous fluid”,J.Fluid Mech., 25(3),591-592(1966). 20 Zapryanov,Z.,Tabakova,S.,Dynamics of Bubbles,Drops and Rigid Particles,Kluwer Academic,Dordrecht,338,343(1999). 21 Reeks,M.W.,McKee,S.,“The dispersive effects of basset history forces on particle motion in a turbulent flow”,Phys.Fluids,27(7), 1573-1582(1984). 22 Sokolichin,A.,Eigenberger,G.,Lapin,A.,“Simulation of buoyancy driven bubbly flow:Established simplifications and open questions”, AIChE J.,50(1),24-45(2004). 23 You,C.F.,Qi,H.Y.,Xu,X.C.,“Progress in the Basset force research and its application”,Chinese Journal of Applied Mechanics,19(2), 31-33(2002).(in Chinese) 24 Drew,D.A.,Lahey,R.T.Jr.,“The virtual mass and lift force on a sphere in rotating and straining flow”,Int.J.Multiphase Flow,13 (1),113-121(1987). 25 Tomiyama,A.,Sou,A.,Zun,I.,Kanami,N.,Sakaguchi,T.,“Effects of Eötvös number and dimensionless liquid volumetric flux on lateral motion of a bubble in a laminar duct flow”,In:Proceedings of the 2nd International Conference on Multiphase Flow Serizawa,A., Fukano,T.,Bataille,J.,eds.,Elsevier,Amsterdam,3-15(1995). 26 Tomiyama,A.,Tamai,H.,Zun,I.,Hosokawa,S.,“Transverse migration of single bubbles in simple shear flows”,Chem.Eng.Sci.,57 (11),1849-1858(2002). 27 Lahey,Jr.R.T.,Lopez de Bertodano,M.,Jones,Jr.O.C.,Buscaglia, G.,“Phase distribution in complex geometry conduits”,Nucl.Eng. Design,141(1/2),177-201(1993). 28 Antal,S.P.,Lahey,Jr.R.T.,Flaherty,J.E.,“Analysis of phase distribution in fully developed laminar bubbly two-phase flow”,Int.J. Multiphase Flow,17(5),635-652(1991). 29 Zhang,L.,Yang,C.,Mao,Z.S.,“Unsteady motion of a single bubble in highly viscous liquid and empirical correlation of drag coefficient”,Chem.Eng.Sci.,63(8),2099-2106(2008). 30 Zhang,L.,Yang,C.,Mao,Z.S.,“Unsteady motion of a single bubble in non-Newtonian liquids and empirical correlation of drag coefficient”,Ind.Eng.Chem.Res.,47(23),9767-9772(2008). Pan,T.W.,Joseph,D.D.,Bai,R.,Glowinski,R.,Sarin,V.,“Fluidization of 1204 spheres:Simulation and experiment”,J.Fluid Mech., 451,169-191(2002). 32 Li,J.,Kuipers,J.A.M.,“Gas-particle interactions in dense gas-fluidized beds”,Chem.Eng.Sci.,58(3-6),711-718(2003). 33 Zinchenko,A.Z.,Davis,R.H.,“An efficient algorithm for hydrodynamical interaction of many deformable drops”,J.Comput.Phys., 157(2),539-587(2000). 34 Happel,J.,“Viscous flow in multi-particle systems:Slow motion of fluids relative to beds of spherical particles”,AIChE J.,4(2),197-201 (1958). 35 Happel,J.,Brenner,H.,Low Reynolds Number Hydrodynamics, 2nd edition,Noordhoff,Leydon the Netherlands(1973). 36 Chhabra,R.P.,Bubbles,Drops,and Particles in Non-Newtonian Fluids,2nd edition,Taylor Francis,300-303(2007). 37 Mao,Z.S.,“Numerical simulation of viscous flow through spherical particle assemblage with the modified cell model”,Chin.J.Chem. Eng.,10(2),149-162(2002). 38 Mao,Z.S.,Wang,Y.F.,“Numerical simulation of mass transfer in a spherical particle assemblage with the cell model”,Powder Technol., 134(1/2),145-155(2003). 39 LeClair,B.P.,Hamielec,A.E.,“Viscous flow through particleassemblages at intermediate Reynolds numbers—A cell model for transport in bubbles swarms”,Can.J.Chem.Eng.,49(6),713-720 (1971). 40 Sankaranarayanan,K.,Sundaresan,S.,“Lift force in bubbly suspensions”,Chem.Eng.Sci.,57(17),3521-3542(2002). 41 Mao,Z.S.,Chen,J.Y.,“Numerical approach to the motion and external mass transfer of a drop swarm by the cell model”,In:International Solvent Extraction Conference(ISEC'2002),Sole,K.C.,Cole, P.M.,Preston,J.S.,Robinson,D.J.,eds.,South African Institute of Mining and Metallurgy,Johannesburg,South Africa,227-232(2002). 42 Mao,Z.S.,Chen,J.Y.,“An attempt to improve the cell model for motion and external mass transfer of a drop in swarms at intermediate Reynolds numbers”,In:International Solvent Extraction Conference(ISEC'2005),Fei,W.Y.,Liu,H.Z.,Yan,C.H.,eds.,Beijing, A417(2005). 43 Kumar,A.,Hartland,S.,“Gravity settling in liquid/liquid dispersions”,Can.J.Chem.Eng.,63(3),368-376(1985). 44 Wen,C.Y.,Yu,Y.H.,“Mechanics of fluidization”,Chem.Eng.Prog. Symp.Ser.,62,100-111(1966). 45 Oey,R.S.,Mudde,R.F.,van den Akker,H.E.A.,“Sensitivity study on interfacial closure laws in two-fluid bubbly flow simulations”, AIChE J.,49(7),1621-1636(2003). 46 Koch,D.L.,Hill,R.J.,“Inertial effects in suspension and porous-media flows”,Ann.Rev.Fluid Mech.,33,619-647(2001). 47 Pan,Y.,Dudukovic,M.P.,Chang,M.,“Numerical Investigation of gas-driven flow in 2-D bubble columns”,AIChE J.,46(3),434-449 (2000). 48 Li,J.H.,Kwauk,M.S.,“Exploring complex systems in chemical engineering—The multi-scale methodology”,Chem.Eng.Sci.,58(2), 521-535(2003). |