On mechanism of enhancement of two-phase flow heat transfer in a narrow channel

Z. L. Yang, B. Palm, Ivan Kazachkov, B. Sehgal
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引用次数: 3

Abstract

In this paper, several different aspects of thermal dynamics of two-phase flow in a narrow channel have been addressed and analysed. According to the flow regime classification of two-phase flow in a narrow channel, only Taylor bubble flow and annular flow with thin liquid film are considered since they are of most interest for practical applications. The hydrodynamics of Taylor bubbles in a narrow channel is simulated by an advanced CFD method for two-phase flow - Lattice-Boltzmann method. The present numerical simulation provides reasonable pictures of Taylor bubble dynamics which agrees qualitatively well with analytical solutions and experimental observations. More importantly, the simulation results show that several vertices near the head and meniscus of the Taylor bubble appear. Experimental study is performed to study the condensation heat transfer inside a square channel. The experimental results show that significant enhancement of heat transfer is achieved in comparison with the predictions by Nusselt's correlation. This indicated clearly that the capillary force is playing an important role in redistribution of the film thickness inside the channel. An instability analysis is also performed to investigate the dynamics of the thin film flow in a narrow channel. The analytical solution for a narrow gap channel shows that there is no growing wave on the film surface from perturbation, all the kinematic waves coming from perturbations on the film surface are convoyed by vapor flow without growing or decreasing since the liquid film is too thin. The wave structure of the interface of two-phase flow could enhance significantly the heat transfer between the liquid film and heated wall.
窄通道内加强两相流换热的机理研究
本文讨论和分析了窄通道中两相流的热动力学的几个不同方面。根据窄通道两相流的流型分类,仅考虑泰勒泡流和薄液膜环空流,因为它们在实际应用中最有意义。采用一种先进的两相流CFD方法——格点-玻尔兹曼方法,对Taylor气泡在狭窄通道中的流体力学进行了数值模拟。本文的数值模拟提供了合理的泰勒气泡动力学图像,与解析解和实验观测结果在质量上很好地吻合。更重要的是,仿真结果表明,泰勒气泡的头部和半月板附近出现了几个顶点。对方形通道内的冷凝换热进行了实验研究。实验结果表明,与Nusselt相关预测相比,传热得到了显著增强。这清楚地表明毛细力在通道内薄膜厚度的重新分布中起着重要的作用。本文还对薄膜在窄通道中的流动动力学进行了不稳定性分析。窄间隙通道的解析解表明,由于液膜太薄,扰动在膜表面不产生生长波,所有来自膜表面扰动的运动波都被汽流所传递,既不增长也不减少。两相流界面的波动结构可以显著增强液膜与受热壁面之间的换热。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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