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Heat transfer characteristics of gas–liquid flow in horizontal rectangular micro-channels

机译:水平矩形微通道中气液流动的传热特性

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An experimental study of heat transfer characteristics of air–water flow in horizontal micro-channels was carried out in this work. The gas–liquid mixture from a y-shaped mixing chamber was forced to pass through a plenum inlet and entered 21 parallel rectangular micro-channels 40 mm long in the direction of flow. Each channel had a width and a depth of 0.45 and 0.41 mm, respectively. The test runs were done at a heat load of 80 W, with superficial Reynolds numbers of gas and liquid ranging between 54–142 and 131–373, respectively. A Stereozoom microscope and camera system were employed to conduct flow visualization. To explore the dependence of a Nusselt number on the flow characteristics, two inlet sections with different designs were used in this work. The experiments revealed that the formation of small gas slugs instead of gas core flow involves an increase in Nusselt numbers. In this work, the gas–liquid flow gave heat transfer enhancement up to 80% over the liquid flow.
机译:在这项工作中进行了水平微通道中空气-水流传热特性的实验研究。来自y形混合室的气液混合物被迫通过气室入口,并进入沿流动方向长40 mm的21个平行矩形微通道。每个通道的宽度和深度分别为0.45和0.41 mm。测试运行在80 W的热负荷下进行,气体和液体的表面雷诺数分别在54–142和131–373之间。使用Stereozoom显微镜和摄像头系统进行流量可视化。为了探究努塞尔数对流动特性的依赖性,在这项工作中使用了两个设计不同的入口段。实验表明,形成小的气团而不是气芯流涉及努塞尔特数的增加。在这项工作中,气液流动使传热比液流提高了80%。

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