Effect of surfactants on hydrodynamics characteristics of bubble in shear thinning fluids at low Reynolds number

被引:6
作者
Li Shao-bai [1 ]
Fan Jun-geng
Li Run-dong
Wang Lei
Luan Jing-de
机构
[1] Shenyang Aerosp Univ, Liaoning Key Lab Clean Energy, Shenyang 110136, Liaoning, Peoples R China
基金
中国国家自然科学基金;
关键词
surfactant; single bubble; shear thinning fluids; velocity; drag coefficient; NON-NEWTONIAN LIQUIDS; GAS-BUBBLES; RISE VELOCITY; TERMINAL VELOCITY; MASS-TRANSFER; MOTION; SHAPE; DROP; DRAG;
D O I
10.1007/s11771-018-3785-9
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
In this study, the effects of surfactants on the hydrodynamic characteristics of bubbles in shear-thinning fluids at low Reynolds number (Re < 50) are investigated. The bubble terminal velocity and drag coefficient of bubble in clean and contaminated carboxymethylcellulose (CMC) solutions are obtained using a high-speed camera for examining differences. The results show that the existence of surfactant could reduce the terminal velocity of bubble at small volume (0.25wt% CMC: < 100 mm(3); 0.50wt% CMC: < 110 mm(3)), attributed to stiffening the bubble interface. However, this negative effect decreases and finally disappears with increasing bubble volume. The drag coefficient curves of the bubble in contaminated CMC solution exhibit behavior similar to that exhibited by a solid sphere at Re < 10, indicating that internal circulation flow is absent at the bubble interface as compared to that in clean CMC solution. However, for 10 < Re < 40, a transition of drag curve from 24/Re to 16/Re in contaminated CMC solution is observed, which is easy at low SDS concentrations and high CMC concentrations.
引用
收藏
页码:805 / 811
页数:7
相关论文
共 28 条
[1]   Effect of bubble contamination on rise velocity and mass transfer [J].
Alves, SS ;
Orvalho, SP ;
Vasconcelos, JMT .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (01) :1-9
[2]   Shape and terminal velocity of single bubble motion: a novel approach [J].
Bozzano, G ;
Dente, M .
COMPUTERS & CHEMICAL ENGINEERING, 2001, 25 (4-6) :571-576
[3]  
Clift R., 2005, Bubbles, drops, and particles
[4]   THE AXISYMMETRIC RISE OF A SPHERICAL BUBBLE AT THE EXIT OF AN ORIFICE IN THE PRESENCE OF A STAGNANT CAP OF INSOLUBLE SURFACTANTS [J].
DAGAN, Z ;
YAN, ZY ;
SHEN, HX .
JOURNAL OF FLUID MECHANICS, 1988, 190 :299-319
[5]   Hydrodynamic characteristics of free rise of light solid particles and gas bubbles in non-Newtonian liquids [J].
Dewsbury, K ;
Karamanev, D ;
Margaritis, A .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) :4825-4830
[6]   An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient [J].
Fan Wenyuan ;
Ma Youguang ;
Jiang Shaokun ;
Yang Ke ;
Li Huaizhi .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2010, 132 (02) :0213051-0213057
[7]   Effects of surfactant on terminal velocity of a Taylor bubble in a vertical pipe [J].
Hayashi, Kosuke ;
Tomiyama, Akio .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2012, 39 :78-87
[8]   RISE OF GAS-BUBBLES IN QUIESCENT LIQUIDS [J].
KARAMANEV, DG .
AICHE JOURNAL, 1994, 40 (08) :1418-1421
[9]   Development of steady state adsorption distribution over interface of a bubble rising in solutions of n-alkanols (C5, C8) and n-alkyltrimethylammonium bromides (C8, C12, C16) [J].
Krzan, M. ;
Zawala, J. ;
Malysa, K. .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2007, 298 (1-2) :42-51
[10]   Bubble formation and bubble rise velocity in gas-liquid systems: A review [J].
Kulkarni, AA ;
Joshi, JB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (16) :5873-5931