Computational analysis of a subcooled boiling flow with a one-group interfacial area transport equation

被引:17
作者
Bae, Byoung-Uhn [2 ]
Yoon, Han-Yong [1 ]
Euh, Dong-Jin [1 ]
Song, Chul-Hwa [1 ]
Park, Goon-Cherl [2 ]
机构
[1] Korea Atom Energy Res Inst, Taejon, South Korea
[2] Seoul Natl Univ, Dept Nucl Engn, Seoul, South Korea
关键词
CFD code; interfacial area transport equation; SMAC algorithm; subcooled boiling flow; bubble departure diameter model;
D O I
10.3327/jnst.45.341
中图分类号
TL [原子能技术]; O571 [原子核物理学];
学科分类号
0827 ; 082701 ;
摘要
For a multidimensional analysis of a two-phase flow, a computational fluid dynamics (CFD) code was developed with the implementation of an interfacial area transport equation that is beneficial for dynamically estimating the interfacial area concentration (IAC). The code structure was based on the two-fluid model and the Simplified Marker and Cell (SMAC) algorithm. The SMAC algorithm was extended to a two-phase flow simulation with a phase change. Various well-known constitutive models regarding boiling, condensation, and nondrag forces have been implemented into the code. To verify the robustness of the code to predict wall boiling and void propagation phenomena, a subcooled boiling test in a vertical annulus channel was analyzed as a benchmark problem. As the analysis results, a model for bubble departure diameter on the heated wall was identified as the principal factor for subcooled boiling phenomena, and the limitation of the current departure diameter models under a low-pressure condition resulted in a deviation of the void fraction and IAC when compared with the results of the experiment. It is necessary that the research on the interfacial area transport equation focuses on modeling reliable source terms for the boiling mechanism as a future work.
引用
收藏
页码:341 / 351
页数:11
相关论文
共 27 条
[1]  
AEA, 1997, CFX 4 SOLV MAN
[2]  
AMSDEN AA, 1971, LA4370 LOS AL SCI LA
[3]  
[Anonymous], P 5 INT C MULT FLOW
[4]   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
[5]  
BAE BU, 2007, P 2007 INT C ADV NUC
[6]   On the modelling of population balance in isothermal vertical bubbly flows - Average bubble number density approach [J].
Cheung, Sherman C. P. ;
Yeoh, G. H. ;
Tu, J. Y. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2007, 46 (08) :742-756
[7]   ANALYSIS OF VIRTUAL MASS EFFECTS IN 2-PHASE FLOW [J].
DREW, D ;
CHENG, L ;
LAHEY, RT .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1979, 5 (04) :233-242
[8]  
Ferziger Joel H, 2002, Computational Methods for Fluid Dynamics, V3
[9]   Development of one-group interfacial area transport equation in bubbly flow systems [J].
Hibiki, T ;
Ishii, M .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2002, 45 (11) :2351-2372
[10]  
Incropera FrankP., 2002, INTRO HEAT TRANSFER, V4th