On the modelling of population balance in isothermal vertical bubbly flows - Average bubble number density approach

被引:71
作者
Cheung, Sherman C. P.
Yeoh, G. H.
Tu, J. Y. [1 ]
机构
[1] RMIT Univ, Sch Aerosp Mech & Mfg Engn, Melbourne, Vic 3083, Australia
[2] Australian Nucl Sci & Technol Org, Menai, NSW 2234, Australia
基金
澳大利亚研究理事会;
关键词
population balance; gas-liquid flow; CFD; model validation;
D O I
10.1016/j.cep.2006.10.004
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
To model the spatial evolution of the geometrical structure of the gas bubbles in isothermal vertical bubbly flow conditions, the population balance approach has been employed and merged with the three-dimensional two-fluid model. The population balance is realized by incorporating an average bubble number density transport equation into a commercial computational fluid dynamics (CFD)codeANSYS CFX 10. The coalescence and breakage effects of the gas bubbles are formulated according to the bubble coalescence by random collision driven by turbulence and wake entrainment while for bubble breakage by the impact of turbulent eddies. Three models representing these coalescence and breakage mechanisms proposed by Wu et al. [1], Hibiki and Ishii [2] and Yao and Morel [3] are assessed. Local radial distributions of the five primitive variables in bubbly flows: void fraction, Sauter mean diameter, interfacial area concentration, and gas and liquid velocities, are compared with two experimental data of Liu and Bankoff [4,5] and Hibiki et al. [6]. Close agreements between the predictions and measurements demonstrated the capability of the average bubble number density transport equation in modelling bubbly flow conditions. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:742 / 756
页数:15
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