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首页> 外文期刊>International Journal of Heat and Mass Transfer >The effect of heating area orientation on flow boiling performance in microchannels heat sink under subcooled condition
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The effect of heating area orientation on flow boiling performance in microchannels heat sink under subcooled condition

机译:过冷条件下加热区取向对微通道散热器流沸腾性能的影响

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Subcooled flow boiling heat transfer experiments were conducted in this work in order to investigate the effect of the heating area orientation of microchannels heat sink on flow boiling heat transfer and pressure drop characteristics. The flow boiling heat transfer experiments were conducted in a 31 parallel "U" shaped microchannels (width 305 μm and depth 290 μm) heat sink with deionized water as the working fluid. The tests were conducted for different orientations such as, Horizontal upward facing (HU), Horizontal with heating area vertically aligned (HV), Vertical with up flow (VUF), Vertical with downflow (VDF) and Horizontal downward facing (HD) in a forced convection loop with volume flow rate of 50 ml/ min, 100 ml/min and 150 ml/min. From the experimental results, it was observed that the performances of the heat sink under all orientation conditions were found to be almost identical except the vertical downflow orientation (VDF). The critical heat flux values are found to be less in the case of vertical down-flow orientation. In the case of vertical downflow orientation, the critical heat flux values corresponding to 50,100 and 150 ml/min flow rate were 44.1 W/cm2, 74 W/cm2 and 99.3 W/cm2 respectively. For VDF orientation the buoyancy force acts on bubbles against the flow direction. Consequently, the bubbles were built up and merge each other due to the difficulty in draining and reversed flow was created with less heat flux input. The total pressure drop observed to be more for vertical downflow orientation compared to other orientations. Significant pressure fluctuations were observed during flow boiling in microchannels with VDF and HD orientations at low flow rates. The percentage reduction in effective heat flux value at the incipience of critical heat flux (CHF) in VDF orientation for flow rate of 50, 100 and 150 ml/min were 13%, 10.30% and 7.40%, and the corresponding percentage reduction in maximum outlet heat transfer coefficient was 30%, 23% and 19% respectively.
机译:在这项工作中进行过冷流沸腾传热实验,以研究微通道散热器的加热区域取向对流沸腾传热和压降特性的影响。流动沸腾传热实验是在31个平行的“ U”形微通道(宽305μm,深290μm)的散热器中进行的,其中去离子水为工作流体。测试针对不同的方向进行,例如,水平方向朝上(HU),水平加热区域垂直对齐(HV),垂直向上流动(VUF),垂直向下流动(VDF)和水平向下(HD)强制对流回路,体积流量分别为50 ml / min,100 ml / min和150 ml / min。从实验结果可以看出,除垂直向下流动方向(VDF)外,在所有方向条件下散热器的性能几乎相同。发现在垂直向下流动的情况下,临界热通量值较小。在垂直向下流动的情况下,对应于50,100和150 ml / min流量的临界热通量值分别为44.1 W / cm2、74 W / cm2和99.3 W / cm2。对于VDF定向,浮力逆着流向作用在气泡上。因此,由于排液困难,气泡堆积并相互融合,并以较少的热通量输入产生了反向流动。与其他方向相比,垂直向下流动方向的总压降更大。在低流速下,在具有VDF和HD取向的微通道中,在沸腾过程中观察到明显的压力波动。在流速为50、100和150 ml / min的情况下,在VDF方向上临界热通量(CHF)出现时,有效热通量减少的百分比分别为13%,10.30%和7.40%,最大减少相应的百分比出口传热系数分别为30%,23%和19%。

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