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Numerical study of adiabatic two-phase flow patterns in vertical rectangular narrow channels

机译:垂直矩形窄沟道中绝热两相流动模式的数值研究

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The current paper investigates an upward two-phase flow of air-water mixture in vertical narrow rectangular channels with two different cross-sectional dimensions of 25 x 5 mm and 25 x 2 mm respectively by using VOF (Volume of Fluid) model. To facilitate the simulations of different flow patterns, a simple and practical inlet condition, which is validated by experimental results, is employed. In the VOF model, the inlet condition will make the gas phase to be air layers, and due to the entrainment effect, the layers would coalescent and break up to small bubbles. The simulation results reveal that the main flow patterns of the two-phase flow in narrow channels are bubbly flow, slug flow, churn-turbulent flow and annular flow, and the void fraction distributions of those flow patterns are quite different. The void fraction of bubbly flow is below 0.3, which is consistent with published literatures. As the Taylor bubbles are located at the center of the flow channel and the slug flow is intermittent, the void fraction of slug flow is more evenly distributed in the center. The flow pattern map has been drafted under various air-water superficial velocities. The central region of the annular flow is gas core entrained liquid droplets, thus the void fraction is almost constant in the central region. The two-phase flow pattern map of a vertical rectangular channel shows that the range of annular flow in the channel is larger, while the scopes of slug flow and bubbly flow in the channel are smaller in comparison with the flow pattern map of tube. In addition, the transitional boundaries between flow patterns occur at smaller gas velocity than those in the tube. While compared the 2 mm gap rectangular channel with the 5 mm ones, it is found that with the gap size reducing, the flow pattern transition boundary shifts to the left. (C) 2016 Elsevier Ltd. All rights reserved.
机译:目前纸张通过使用vof(流体的体积)模型,在垂直窄矩形通道中调查了垂直窄矩形通道中的空气 - 水混合物的向上两相流,分别为25×5mm和25×2mm。为了便于模拟不同的流动模式,采用了通过实验结果验证的简单实用的入口条件。在VOF模型中,入口状况将使气相成为空气层,并且由于夹带效果,层将结束并分裂到小气泡。仿真结果表明,窄通道中的两相流的主流量模式是起泡流动,块状流动,搅拌湍流和环形流动,并且这些流动模式的空隙分量分布非常不同。气泡流量的空隙率低于0.3,这与公开的文献一致。当泰勒气泡位于流动通道的中心并且块流是间歇性的时,在中心的空隙流动的空隙率均匀分布。在各种空气浅表速度下,流动模式图已起草。环形流动的中心区域是气体夹带液滴,因此在中心区域中空隙部分几乎恒定。垂直矩形通道的两相流动图案图表明通道中的环形流程范围更大,而与管的流动图案图相比,槽中的块流和气泡流动的范围较小。另外,流动模式之间的过渡边界发生在比管中较小的气体速度下。虽然将2 mm间隙矩形通道与5mm的间隙矩形相比进行比较,但发现具有间隙尺寸减小,流动模式转换边界向左移动。 (c)2016 Elsevier Ltd.保留所有权利。

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