3-D computational investigation and experimental validation of effect of shear-lift on two-phase flow and heat transfer characteristics of highly subcooled flow boiling in vertical upflow

被引:33
|
作者
Lee, Jeongmin [1 ]
O'Neill, Lucas E. [1 ]
Mudawar, Issam [1 ]
机构
[1] Purdue Univ, Sch Mech Engn, PU BTPFL, 585 Purdue Mall, W Lafayette, IN 47907 USA
基金
美国国家航空航天局;
关键词
Two-phase flow; Subcooled flow boiling; Shear-lift force; CFD; PRESSURE-DROP; NUMERICAL-SIMULATION; MASS VELOCITY; INLET QUALITY; ORIENTATION; CONVECTION; CHANNEL; BUBBLE; FORCE; FLUX;
D O I
10.1016/j.ijheatmasstransfer.2019.119291
中图分类号
O414.1 [热力学];
学科分类号
摘要
The present study is focused on development of a 3-D computational approach to predict highly subcooled nucleate flow boiling in vertical upflow. Investigation of existing computational methodology based on Volume of Fluid (VOF) approach revealed fundamental weaknesses in modeling multiphase flows, which stems mostly from inadequate representation of shear-lift force on bubbles. A user defined function is adopted which provides detailed information relating to this important effect, and computed results are validated through comparison with experimental results and analytic predictions of single bubble trajectory. The computational method is then used to model the entire flow field for subcooled flow boiling in a rectangular channel heated on two opposite walls, and predictions are validated against FC-72 experimental data for four different mass velocities. Overall, computationally predicted interfacial behavior, flow pattern, and heat transfer parameters (wall temperature and heat transfer coefficient) show good agreement with experimental data. The model is also shown highly effective at predicting local phenomena (velocity and temperature profiles) not easily determined through experiments. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页数:19
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