Influence of operating conditions and liquid phase viscosity with volume of fluid method on bubble formation process

被引:21
作者
Abbassi, W. [1 ]
Besbes, S. [1 ]
El Hajem, M. [2 ]
Ben Aissia, H. [1 ]
Champagne, J. Y. [2 ]
Jay, J. [3 ]
机构
[1] Natl Sch Engineers, Dept Energy Engn, Res Unit Metrol & Energy Syst, Rd Ouerdanine, Monastir 5000, Tunisia
[2] Natl Inst Appl Sci INSA Lyon, Lab Fluid Mech & Acoust LMFA, 20 Av A Einstein, F-69621 Villeurbanne, France
[3] Natl Inst Appl Sci INSA Lyon, Thermal Ctr Lyon CETHIL, 20 Av A Einstein, F-69621 Villeurbanne, France
关键词
Bubble formation; Shape; Aspect ratio; Formation time; Volume of fluid; CONSTANT FLOW CONDITIONS; LEVEL SET METHODS; SUBMERGED ORIFICES; SURFACE-TENSION; AIR-BUBBLES; NUMERICAL-SIMULATION; 2-COMPONENT SYSTEMS; SHAPE OSCILLATIONS; VISCOUS-LIQUIDS; GAS BUBBLE;
D O I
10.1016/j.euromechflu.2017.04.001
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
In this paper, a numerical study of air bubble formation and detachment in water (S-1) and in glycerin solutions (S-2 and S-3) was investigated using the volume of fluid (VOF) method. The full formation process was studied under the effect of operating conditions such as wettability of the orifice plate (static contact angle theta(s)), orifice diameter and orifice air velocity. In addition, the influence of the viscosity of the liquid phase was examined. The numerical simulations were carried out for different orifice velocities satisfying the quasi-static bubble growth condition at low Capillary and Bond numbers. Under such conditions, the surface tension effect is dominant over viscous drag and buoyancy effects. The bubble growth at different instants predicted by the VOF simulation was experimentally validated in water. During the expansion/elongation stage significant bubble shape oscillations have been observed by the simulation. In water, bubble shape is mainly dominated by inertial and surface tension forces, and the influence caused by the viscous drag force could be neglected. However, when the viscosity of the solution increases, the bubble shape oscillations can be reduced due to the effect of viscous drag force. (C) 2017 Elsevier Masson SAS. All rights reserved.
引用
收藏
页码:284 / 298
页数:15
相关论文
共 49 条
[21]  
Gibbs J.W., 1906, SCI PAPERS THERMODYN, V1, P1961
[22]   Axisymmetric bubble pinch-off at high Reynolds numbers -: art. no. 194501 [J].
Gordillo, JM ;
Sevilla, A ;
Rodríguez-Rodríguez, J ;
Martínez-Bazán, C .
PHYSICAL REVIEW LETTERS, 2005, 95 (19)
[23]   VOLUME OF FLUID (VOF) METHOD FOR THE DYNAMICS OF FREE BOUNDARIES [J].
HIRT, CW ;
NICHOLS, BD .
JOURNAL OF COMPUTATIONAL PHYSICS, 1981, 39 (01) :201-225
[24]   Study of bubble formation under constant flow conditions [J].
Jamialahmadi, M ;
Zehtaban, MR ;
Müller-Steinhagen, H ;
Sarrafi, A ;
Smith, JM .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2001, 79 (A5) :523-532
[25]   Experimental study of bubble formation at metal porous spargers: Effect of liquid properties and sparger characteristics on the initial bubble size distribution [J].
Kazakis, N. A. ;
Mouza, A. A. ;
Paras, S. V. .
CHEMICAL ENGINEERING JOURNAL, 2008, 137 (02) :265-281
[26]   Effect of frother on initial bubble shape and velocity [J].
Kracht, W. ;
Finch, J. A. .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 2010, 94 (3-4) :115-120
[27]  
Kumar R., 1970, Advances in Chemical Engineering, V8, P256
[28]   MODELING MERGING AND FRAGMENTATION IN MULTIPHASE FLOWS WITH SURFER [J].
LAFAURIE, B ;
NARDONE, C ;
SCARDOVELLI, R ;
ZALESKI, S ;
ZANETTI, G .
JOURNAL OF COMPUTATIONAL PHYSICS, 1994, 113 (01) :134-147
[29]   Modelling the bubble formation dynamics in non-Newtonian fluids [J].
Li, HZ ;
Mouline, Y ;
Midoux, N .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (03) :339-346
[30]   Experimental studies on the shape and motion of air bubbles in viscous liquids [J].
Liu, Liu ;
Yan, Hongjie ;
Zhao, Guojian .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2015, 62 :109-121