Experimental and computational investigation of flow boiling in microgravity. (February 2022)

• Record Type: Journal Article
• Authors: Lee, Jeongmin; Mudawar, Issam; Hasan, Mohammad M.; Nahra, Henry K.; Mackey, Jeffrey R.
• Is Part Of: International journal of heat and mass transfer. Volume 183:Part C(2022)
• Publication Date: 2022-02
• Subjects: Two-phase cooling -- Flow boiling -- CFD -- Microgravity; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2021.122237
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: A 3-D CFD model is presented for prediction of interfacial behavior in microgravity flow boiling. The CFD method is based on the volume of fluid (VOF) model and incorporates the important influence of shear-lift force. The model accurately predicts both measured wall temperature and interfacial structure. CFD method is equally effective in tackling terrestrial gravity and microgravity conditions. Abstract: This study explores use of Computational Fluid Dynamics (CFD) to predict near-saturated flow boiling of FC-72 in microgravity. The computational method employs transient analysis to predict detailed interfacial behavior and heat transfer characteristics along a rectangular channel heated along two opposite walls. Predicted results are validated against experimental temperature measurements and high-speed video images captured during a series of parabolic aircraft maneuvers for three sets of operating conditions which include variations of both mass velocity and wall heat flux. The computational method is based on the multi-phase volume of fluid (VOF) model, which is combined with appropriate phase change and turbulence models, and accounts for both shear-lift force on bubbles and conjugate heat transfer along the heating walls. A key advantage of the CFD method is ability to capture details that are very difficult to measure experimentally, including detailed spatial variations of bubble shape, void fraction, mixture fluid temperature, liquid velocity, and vapor velocity, results for which are presented for each of the three test cases. Different flow regimes predicted along the heated length exhibit a number of dominant mechanisms including bubble nucleation, bubble growth, coalescence, vapor blankets, interfacial waviness, and residual liquid sub-layer, all of which agree well with experiment. Vapor velocity is shown to increase appreciably along the heated length because of increased void fraction, while liquid velocity experiences large fluctuations. Non-equilibrium effects are accentuated with increasing mass velocity, contributing minor deviations of fluid temperature from simulations compared to those predicted by the analytical method. Predicted wall temperature is fairly uniform in the middle of the heated length but increases in the entrance region, due to sensible heat transfer in the subcooled liquid, and decreases toward the exit, mostly because of flow acceleration resulting from increased void fraction.