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

机译:垂直矩形窄通道中绝热两相流场的数值研究

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摘要

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:本文利用VOF(流体体积)模型研究了在垂直狭窄的矩形通道中空气-水混合物的向上两相流动,垂直矩形通道具有两个不同的横截面尺寸,分别为25 x 5 mm和25 x 2 mm。为了便于模拟不同的流态,采用了简单而实用的进气条件,该条件已通过实验结果进行了验证。在VOF模型中,入口条件将使气相成为空气层,由于夹带效应,这些层会聚结并破裂成小气泡。仿真结果表明,窄通道内两相流的主要流态为气泡流,团状流,搅动湍流和环形流,且这些流态的空隙率分布差异很大。气泡流的空隙率低于0.3,这与已发表的文献一致。由于泰勒气泡位于流道的中心,并且团状流是断续的,所以团状流的空隙率更加均匀地分布在中心。在各种空气-水表观速度下绘制了流型图。环形流的中心区域是夹带气芯的液滴,因此空隙率在中心区域几乎恒定。垂直矩形通道的两相流型图显示,与管型流型图相比,通道中环形流的范围较大,而通道中的弹状流和气泡流的范围较小。另外,流动模式之间的过渡边界以比管中的气体速度小的气体速度出现。将2 mm间隙矩形通道与5 mm间隙矩形通道进行比较时,发现随着间隙尺寸的减小,流型转变边界向左移动。 (C)2016 Elsevier Ltd.保留所有权利。

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