Classification of bubbles in vertical gas-liquid flow: Part 2-A model evaluation

被引:15
作者
Cheung, S. C. P. [1 ]
Yeoh, G. H. [2 ,3 ]
Qi, F. S. [1 ,4 ]
Tu, J. Y. [1 ]
机构
[1] RMIT Univ, SAMME, Melbourne, Vic 3083, Australia
[2] ANSTO, Kirrawee Dc, NSW 2232, Australia
[3] Univ New S Wales, Sch Mech & Mfg Engn, Sydney, NSW 2052, Australia
[4] Northeastern Univ, Sch Met & Mat, Shenyang 110004, Peoples R China
基金
澳大利亚研究理事会;
关键词
Gas-liquid two-phase flow; Three-fluid model; Two-group average bubble number density; Intra-group mechanisms; Inter-group mechanisms; INTERFACIAL AREA TRANSPORT; DEVELOPED TURBULENT-FLOW; LARGE-DIAMETER PIPE; 2-PHASE FLOW; POPULATION BALANCE; PHASE DISTRIBUTION; HEAT-TRANSFER; COALESCENCE; BREAKUP; DISPERSIONS;
D O I
10.1016/j.ijmultiphaseflow.2011.10.009
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Three-fluid model along with two-group average bubble number density equations have been applied for the classification of bubbles in vertical gas-liquid flow. The current study focused on (i) consideration of three-fluid model transport equations governing the conservation of mass and momentum, (ii) formulation of two-group averaged bubble number density equations, (iii) classification of bubble interaction between spherical bubbles (Group-1) and cap bubbles (Group-2), (iv) consideration of source and sink terms via the proposal of Hibiki and Ishii (Nuclear Engineering and Design 202, 39-76) in the averaged bubble number density equations and (v) assessment by means of the experimental data sets at the bubbly-to-cap flow transition. Reasonable agreement has been achieved between the measured and predicted local and axial distributions of void fraction, interfacial area concentration (IAC) and volume equivalent bubble diameter. This preliminary assessment demonstrated the capability of the current approach in capturing the interfacial transport of bubbly to cap flow transition. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:135 / 147
页数:13
相关论文
共 43 条