Enhancement in thermo hydraulic performance of radially curved microchannel with secondary flow

Nitin Kumar Mamidi, K. Balasubramanian, K. Kupireddi, Chandramohan V.P., Poh-Seng Lee, C. C. Kong
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Abstract

Microchannel-based cooling methods have been found extremely suitable for compact heat exchangers. High rate of heat extraction is always associated with pressure drop penalty which lowers the overall performance of the device. Heat sinks that would deliver high thermal performance at relatively lower pumping are highly desirable. In the present article, curved microchannels with secondary flow channels are numerically investigated to minimize the pressure loss and enhance the heat transfer simultaneously. Uniform heat flux boundary condition with Reynolds number ranging from 100 to 225 is considered for analysis. Seven models having secondary flow channel orientation angles varying from 30° to 42° are compared with radially curved microchannel (RCMC) having central inlet and horizontal radial outlet arrangement. A greater increase in Nu is observed in the secondary channel with a higher orientation angle, primarily attributed to enhanced fluid mixing. Results revealed a maximum Nusselt number increase of 25.72% for RCMC with secondary flow (RCMCSF) when compared to RCMC with reduction in pressure drop penalty at the same time. At a Reynolds number of 100, the RCMCSF 30D demonstrated the maximum pressure loss reduction, which amounted to 23.91% compared to RCMC. The temperature of the wall in contact with the fluid exhibits a decreasing trend with an increase in Reynolds number (Re). This occurrence is attributed to improved fluid mixing, resulting from higher flow rates. The intensified velocity vectors in the cross-plane contribute to this enhanced mixing and subsequent decline in wall temperature. Reduction in average wall temperature up to 3.43°C is noted for RCMCSF when compared to RCMC. Of all the designs considered, radial curved microchannel with a secondary channel orientation angle of 40° shows enhanced thermal hydraulic performance with performance factor equal to 1.31.
利用二次流提高径向弯曲微通道的热液压性能
基于微通道的冷却方法非常适用于紧凑型热交换器。高抽热率总是会带来压降损失,从而降低设备的整体性能。因此,能以相对较低的抽气量提供较高热效率的散热器是非常理想的。本文对带有次级流道的弯曲微通道进行了数值研究,以最大限度地减少压力损失,同时提高传热效果。分析中考虑了雷诺数为 100 到 225 的均匀热流边界条件。将次级流道方向角从 30° 到 42° 不等的七个模型与具有中心入口和水平径向出口布置的径向弯曲微通道(RCMC)进行了比较。在取向角越大的次级流道中,Nu 的增幅越大,这主要归因于流体混合的增强。结果显示,与 RCMC 相比,带有二次流的 RCMC(RCMCSF)的最大努塞尔特数增加了 25.72%,同时压降减少。在雷诺数为 100 时,与 RCMC 相比,RCMCSF 30D 的压力损失减少幅度最大,达到 23.91%。与流体接触的壁面温度随着雷诺数 (Re) 的增加呈下降趋势。出现这种情况的原因是流速提高后,流体混合得到改善。交叉面上增强的速度矢量促成了这种混合的增强以及随后壁面温度的下降。与 RCMC 相比,RCMCSF 的平均壁温最高降低了 3.43°C。在考虑的所有设计中,二级通道方向角为 40° 的径向弯曲微通道显示出更强的热水力性能,性能系数等于 1.31。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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