CFD modeling of bubble-induced turbulence

被引:162
作者
Rzehak, Roland [1 ]
Krepper, Eckhard [1 ]
机构
[1] Helmholtz Zentrum Dresden Rossendorf, Inst Fluid Dynam, D-01314 Dresden, Germany
关键词
Dispersed gas liquid multiphase flow; Bubble induced turbulence; Euler Euler two fluid model; CFD simulation; Model validation; INTERFACIAL AREA TRANSPORT; GAS-LIQUID; PHASE DISTRIBUTION; TRANSVERSE MIGRATION; SINGLE BUBBLES; VERTICAL PIPE; 2-PHASE FLOW; WALL; DIAMETER; VELOCITY;
D O I
10.1016/j.ijmultiphaseflow.2013.04.007
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Modeling of bubble-induced turbulence in dispersed gas-liquid multiphase flow is an important but still unresolved issue. Aside from its intrinsic interest, turbulence in this type of flow has a strong impact on other important processes like turbulent dispersion of the bubbles and bubble-coalescence and -breakup and thus is a central part of the overall model. Especially the latter require as input values of turbulent kinetic energy and dissipation, which as shown subsequently are not readily obtained from the most common approach to add a bubble-induced contribution to the effective viscosity. This may be overcome by including source terms in the single phase two-equation turbulence models that describe the bubble effects on the liquid turbulence. However, no consensus on the precise form of these terms has been reached yet. We here report a comparison of different models of this type. Special care has been given to the selection of a rather comprehensive set of reference data allowing to qualify the validity of the different models. Conclusions towards best practice guidelines for modeling bubbly turbulence are drawn and needs for further research identified. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:138 / 155
页数:18
相关论文
共 58 条
[1]   ANALYSIS OF PHASE DISTRIBUTION IN FULLY-DEVELOPED LAMINAR BUBBLY 2-PHASE FLOW [J].
ANTAL, SP ;
LAHEY, RT ;
FLAHERTY, JE .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1991, 17 (05) :635-652
[2]  
Burns A.D., 2004, 5 INT C MULT FLOW
[3]   A polydisperse model for bubbly two-phase flow around surface ship [J].
Carrica, PM ;
Drew, D ;
Bonetto, F ;
Lahey, RT .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1999, 25 (02) :257-305
[4]   Eulerian-Eulerian two-fluid model for turbulent gas-liquid bubbly flows [J].
Chahed, J ;
Roig, V ;
Masbernat, L .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2003, 29 (01) :23-49
[5]  
de Bertodano M.A. L., 1992, Turbulent bubbly two-phase ow in a triangular duct
[6]   THE PREDICTION OF 2-PHASE TURBULENCE AND PHASE DISTRIBUTION PHENOMENA USING A REYNOLDS STRESS MODEL [J].
DEBERTODANO, ML ;
LEE, SJ ;
LAHEY, RT ;
DREW, DA .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1990, 112 (01) :107-113
[7]  
DEBERTODANO ML, 1994, J FLUID ENG-T ASME, V116, P128
[8]  
Drew D. A., 1998, Theory of Multicomponent Fluids
[9]   MATHEMATICAL-MODELING OF 2-PHASE FLOW [J].
DREW, DA .
ANNUAL REVIEW OF FLUID MECHANICS, 1983, 15 :261-291
[10]   Effect of bubble diameter on modification of turbulence in an upward pipe flow [J].
Fujiwara, A ;
Minato, D ;
Hishida, K .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2004, 25 (03) :481-488