首页> 外文会议>International conference on nanochannels, microchannels and minichannels;ICNMM2010 >AN EXPERIMENTAL STUDY ON CONVECTIVE BOILING HEAT TRANSFER IN MICRO HEAT EXCHANGERS
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AN EXPERIMENTAL STUDY ON CONVECTIVE BOILING HEAT TRANSFER IN MICRO HEAT EXCHANGERS

机译:微型换热器对流沸腾传热的实验研究

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Attributed to its high heat transfer coefficient, evaporating cooling involving the use of micro heat exchangers is considered a possible thermal management solution for cooling of high heat flux electronic devices. The desire to develop high-performance micro heal exchangers operating in the evaporation regime provides a major motivation for the present work. Methanol evaporated in two micro heat exchangers with chevron flow passages and straight flow passages respectively were tested in the present study. The test results show that the heat transfer coefficient increased with increasing flow rate in both chevron and straight flow passages micro heat exchangers. However, the effect of vapor quality on the heat transfer coefficient in the straight passages heat exchanger is in adverse to that in the chevron passages heat exchanger. The heat transfer coefficient increased with increasing vapor quality in the chevron passages heat exchanger but decreased in the straight passages heat exchanger. The flow visualization through transparent cover heat exchangers showed that the liquid film inside channel is partially dry out in the straight passages heat exchanger. The dryout portion area increased with increasing heating rate and exit vapor quality. This degraded the average heat transfer performance for evaporation in the straight passages heat exchanger. Because of the surface tension effect, the liquid film was dragged at the intersection corner of the upper and lower plate chevron passages. There is no significant dryout portion in the chevron passages heat exchanger. The relation of vapor quality with heat transfer performance in chevron passages heat exchanger is therefore similar to the boiling in a single channel prior to critical heat flux condition.
机译:归因于其高的热传递系数,涉及使用微型热交换器的蒸发冷却被认为是用于冷却高热通量电子设备的可能的热管理解决方案。开发以蒸发方式运行的高性能微热交换器的愿望为当前的工作提供了主要动力。在本研究中,分别测试了在两个分别具有人字形流道和直流道的微型热交换器中蒸发的甲醇。测试结果表明,在人字形和直流通道微型换热器中,传热系数都随着流速的增加而增加。但是,蒸气质量对直通道热交换器中的传热系数的影响与人字形通道热交换器中的相反。人字形通道热交换器中的传热系数随蒸汽质量的增加而增加,而直通道热交换器中的传热系数却减小。通过透明盖式换热器的流动可视化显示,通道内的液膜在直通道换热器中部分变干。干燥部分的面积随着加热速率和出口蒸气质量的增加而增加。这降低了直通道热交换器中蒸发的平均传热性能。由于表面张力的作用,液膜被拖到上和下板人字形通道的相交角处。人字形通道热交换器中没有明显的变干部分。因此,人字形通道换热器中蒸汽质量与传热性能的关系类似于临界热通量条件之前在单个通道中的沸腾。

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