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首页> 外文期刊>Experimental Thermal and Fluid Science: International Journal of Experimental Heat Transfer, Thermodynamics, and Fluid Mechanics >Influence of bubble size on the transition from low-Re bubbly flow to slug flow in a vertical pipe
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Influence of bubble size on the transition from low-Re bubbly flow to slug flow in a vertical pipe

机译:气泡大小对垂直管道中低low气泡流向团状流过渡的影响

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An upward air-water bubbly flow in a pipe was studied experimentally, special attention being paid to the transition from bubbly flow to slug flow. The pipe diameter was 72 mm and the height 18 m. The Reynolds number based on liquid flow was low-to-moderate (U-sl < 0.2 in s(-1)), so that bubble break-up due to turbulence was nearly absent. Three different inlet devices were used, which had a significant influence on the initial bubble size and initial bubble concern ration distribution. The transition from bubbly flow to slug flow was shown to be strongly dependent on the inlet configuration, particularly on the bubble size, A number of theoretical models for the transition from bubbly flow to slug flow were reviewed. The Taitel et al. [2] approach was combined with a bubble-size-dependent critical void-fraction expression of Song et al. [7]. This new formulation for the transition from bubbly flow to slug flow was in good agreement with the measurements. (C) 2002 Elsevier Science Inc. All rights reserved. [References: 11]
机译:通过实验研究了管道中的向上的空气-水气泡流,特别注意从气泡流向段塞流的过渡。管道直径为72毫米,高度为18 m。基于液体流动的雷诺数是低到中度的(U-sl <0.2 in s(-1)),因此几乎没有湍流引起的气泡破裂。使用了三种不同的入口装置,它们对初始气泡大小和初始气泡关注比率分布具有重大影响。结果表明,从气泡流向团状流的过渡强烈依赖于入口构造,尤其是气泡大小。回顾了许多从气泡流向团状流过渡的理论模型。泰特尔等。 [2]方法与Song等人的气泡大小相关的临界空隙率表达组合在一起。 [7]。从气泡流向团状流过渡的新配方与测量结果非常吻合。 (C)2002 Elsevier Science Inc.保留所有权利。 [参考:11]

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