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Distribution of two-phase annular flow at header-channel junctions

机译:联管箱通道交界处的两相环形流分布

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The main objective of this work is to examine the distribution of two-phase annular flow at header-channel junctions simulating the corresponding parts of compact heat exchangers. The parameters considered were mass quality at the inlet of the vertical header and intrusion depth of the horizontal channels into the header wall. The cross-section of the header and the channels were fixed to 24 min x 24 mm and 22 mm x 1.8 mm, respectively. Three different intrusion depths (0, 6 and 12 min beyond the inner wall of the header) were tested for the mass flux and the mass quality ranges of 54-134 kg/m(2) s and 0.2-0.5, respectively. Air and water were used as the test fluids. With zero intrusion-depth, less amount of liquid was separated out through the channels at the rear part. However, with the deeper intrusion (6 and 12 mm), the trend was reversed. The deeper intrusion hindered the liquid to flow into the channels installed at the fore part of the header. Finally, a uniform liquid-flow distribution through the parallel channels could be achieved simply by adjusting the intrusion depth. (C) 2003 Elsevier Inc. All rights reserved. [References: 4]
机译:这项工作的主要目的是研究模拟紧凑型换热器的相应部分的集管通道连接处的两相环形流分布。考虑的参数是垂直集管入口的质量和水平通道进入集管壁的深度。集管和通道的横截面分别固定为24分钟x 24毫米和22毫米x 1.8毫米。测试了三种不同的侵入深度(超出集管箱内壁的0、6和12分钟)的质量通量和质量范围分别为54-134 kg / m(2)s和0.2-0.5。空气和水用作测试流体。侵入深度为零时,较少的液体通过后部的通道被分离出来。但是,随着侵入深度的增加(6和12毫米),这种趋势得到了扭转。较深的侵入阻碍了液体流入安装在集管前端的通道。最后,通过调节侵入深度,可以简单地实现通过平行通道的均匀液体流分布。 (C)2003 Elsevier Inc.保留所有权利。 [参考:4]

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