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Heat transfer enhancement for turbulent flow through blockages with elongated holes in a rectangular channel

机译:传热增强,使湍流通过矩形通道中带有细长孔的堵塞物

摘要

In this thesis, turbulent forced convective heat transfer downstream of blockageswith elongated holes in a rectangular channel was studied.The rectangular channel has a width-to-height ratio of 12:1. The blockages havethe same cross section as that of the channel. The diameter of all elongated holes of theblockages is three quarters of the channel height. The blockages are classified into twodifferent types with two different hole-to-blockage area ratios (ratio of total crosssectionalarea of holes to cross-sectional surface area of the blockage) of 0.5 or 0.6. Foreach hole-to-blockage area ratio, the blockages are again subdivided into three differentcases using three different aspect ratios (hole-width-to-height ratio) which aredetermined by the number of holes four, six, and eight holes per blockage.Experiments for total six different cases of blockages were performed under a uniformwall temperature condition (50C). The experiments were conducted at three differentReynolds numbers of about 7,000, 12,000, and 17,000, respectively. Three copper plateheaters with twenty one embedded thermocouples were used to measure the average heattransfer on the surface of channel walls between two consecutive blockages.Results from this study showed that the blockages with elongated holes enhancethe average heat transfer by up to 5.06 and 4.08 times that by fully developed turbulentflow through a smooth channel at the same Reynolds numbers for small and large holeto-blockage area ratios, respectively. The friction factor ratios for small and large holeto-blockage area ratios of the blockages reached 345 and 89 times, respectively, that byfully developed turbulent flow through a smooth channel at the same Reynolds numbers.TP (Thermal Performance) values varied from 0.65 to 1.11 depending on cases.According to the results, Case L-2, which has six elongated holes and hole-toblockagearea ratio of 0.6, is the best option from the TP point of view. But Case S-2,which also had six elongated holes and hole-to-blockage area ratio of 0.5, can be analternative when more weight should be put on the heat transfer enhancement than TPvalue.
机译:本文研究了矩形通道中带有长孔的阻塞物下游的湍流强迫对流换热。矩形通道的宽高比为12:1。堵塞物的横截面与通道的横截面相同。阻塞物的所有细长孔的直径为通道高度的四分之三。堵塞物分为两种类型,孔与堵塞物的面积比(孔的总截面积与堵塞物的横截面面积之比)为0.5或0.6。对于每个孔与堵塞的面积比,使用三种不同的纵横比(孔宽与高度的比)再次将堵塞分为三个不同的情况,长宽比由每个堵塞的孔数四个,六个和八个确定。在均匀的壁温条件下(50℃)对总共六种不同的堵塞情况进行了分析。实验分别在三个不同的雷诺数分别为7,000、12,000和17,000进行。三个带有21个嵌入式热电偶的铜板式加热器用于测量两个连续堵塞之间通道壁表面的平均传热。研究结果表明,带有细长孔的堵塞将平均传热提高了5.06倍和4.08倍。在相同的雷诺数下,分别通过较小和较大的孔与堵塞面积之比,通过光滑通道充分发展的湍流。在相同的雷诺数下,通过光滑通道充分产生湍流,小孔和大孔堵塞面积比的摩擦系数比分别达到345和89倍.TP(热性能)值从0.65到1.11不等根据结果​​,从TP角度来看,具有六个细长孔且孔与堵塞面积比为0.6的Case L-2是最佳选择。但是,当案例S-2中也有六个细长孔且孔与堵塞的面积比为0.5时,可以替代使用TP值来增加传热效果。

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  • 作者

    Lee Yonghee;

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  • 年度 2007
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  • 正文语种 en_US
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