Particle settling in oil-in-water emulsions

被引:5
作者
Beydoun, D [1 ]
Guang, D [1 ]
Chhabra, RP [1 ]
Raper, JA [1 ]
机构
[1] Univ New S Wales, Sch Chem Engn & Ind Chem, Sydney, NSW 2052, Australia
基金
澳大利亚研究理事会;
关键词
emulsions; sedimentation; settling velocity; drag;
D O I
10.1016/S0032-5910(97)03404-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The sedimentation velocity of precision steel spheres in several oil-in-water emulsions stabilized by a range of commercially available surfactants has been measured. in particular, the interaction between the size distribution of oil droplets, the viscosity of emulsions and the terminal velocity of spheres has been investigated in the Reynolds number range similar to 10 to similar to 1000. When the oil droplets are much smaller than the size of the sedimenting particle, one can treat the emulsion as a continuum fluid and available frameworks can be used for the estimation of the settling velocity. However, the accuracy of this so-called 'continuum' approximation is likely to deteriorate rapidly with increasing droplet size and/or decreasing size of the sedimenting particles. (C) 1998 Elsevier Science S.A. All rights reserved.
引用
收藏
页码:72 / 76
页数:5
相关论文
共 7 条
[1]  
Chhabra R P., 1993, Bubbles, Drops and Particles in Non-Newtonian Fluids
[2]  
Clift R, 1978, Bubbles, drops, and particles, DOI 10.1080/07373939308916817
[3]  
FESAS YP, 1984, INT J MULTIPHASE FLO, V10, P485
[4]  
HABERMAN L, 1958, 1143 DEP NAV
[5]   Wall effect for the fall of spheres in cylindrical tubes at high Reynolds number [J].
Uhlherr, PHT ;
Chhabra, RP .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1995, 73 (06) :918-923
[6]   ACCELERATED SETTLING BY ADDITION OF BUOYANT PARTICLES [J].
WEILAND, RH ;
MCPHERSON, RR .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1979, 18 (01) :45-49
[7]   SEDIMENTATION OF SOLID PARTICLES IN OIL-IN-WATER EMULSIONS [J].
YAN, Y ;
MASLIYAH, JH .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1993, 19 (05) :875-886