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Heat Exchanger Improvement Via Curved Microfluidic Channels: Impacts of Cross-Sectional Geometry and Dean Vortex Strength

机译:通过弯曲的微流体通道改进换热器:横截面几何形状和涡旋强度的影响

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摘要

The efficiency of conventional heat exchangers is restricted by many factors, such as effectiveness of convective heat transfer and the cost of their operation. The current research deals with these issues by developing a novel method for building a lower-cost yet more efficient heat sink. This method involves using a specially designed curved microchannel to utilize the enhanced fluid mixing characteristics of Dean vortices and thus transferring heat efficiently. Numerical models have been employed to investigate the heat transfer enhancement of curved channels over straight equivalents, with the aim of optimizing the heat exchanger design based on the parameters of maximizing heat transfer while minimizing pressure drop and unit cost. A range of cross-sectional geometries for the curved channels was compared, showing significantly higher Nusselt numbers than equivalent straight channels throughout and finding superior performance factors for square, circular, and symmetrical trapezoidal profiles. Due to the difficulty and expense in manufacturing circular microchannels, the relatively simple to fabricate square and symmetrical trapezoidal channels are put forward as the most advantageous designs. The variation of Nusselt number over the length of the channel for a range of different curvatures (and hence Dean numbers) is also examined, showing significantly higher heat transfer occurring in strongly curved channels, especially in areas where the generated Dean vortices are strongest. The variation in Nusselt number was found to form the shape of an "arc." In this way, a relationship between the Dean number and the Nusselt number is characterized and discussed, leading to suggestions regarding optimal microfluidic heat transfer design.
机译:常规热交换器的效率受到许多因素的限制,例如对流传热的效率及其运行成本。当前的研究通过开发一种新颖的方法来构建这些低成本,更高效的散热器来解决这些问题。该方法涉及使用专门设计的弯曲微通道,以利用迪安涡旋增强的流体混合特性,从而有效地传递热量。数值模型已被用于研究弯曲通道在直线当量上的传热增强,目的是基于最大化传热,同时最小化压降和单位成本的参数来优化热交换器设计。比较了弯曲通道的一系列横截面几何形状,显示出与整个等效直线通道相比,努塞尔特数明显更高,并且找到了方形,圆形和对称梯形轮廓的优异性能因子。由于制造圆形微通道的困难和费用,提出相对简单的制造方形和对称梯形通道作为最有利的设计。还检查了在不同曲率范围内Nusselt数在通道长度上的变化(以及由此得出的Dean数),显示出在强烈弯曲的通道中,特别是在生成的Dean涡旋最强的区域中,发生的传热明显更高。发现努塞尔数的变化形成“弧”的形状。这样,表征和讨论了迪安数和努塞尔数之间的关系,从而提出了有关最佳微流体传热设计的建议。

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  • 来源
    《Journal of Heat Transfer》 |2018年第1期|011801.1-011801.9|共9页
  • 作者单位

    Department of Mechanical Engineering, National University of Singapore, 117608, Singapore;

    Department of Mechanical Engineering, National University of Singapore, 117608, Singapore;

    Department of Mechanical Engineering, National University of Singapore, 117608, Singapore;

    Department of Mechanical Engineering, National University of Singapore, 117608, Singapore;

    Department of Mechanical Engineering, National University of Singapore, 117608, Singapore;

    Department of Mechanical Engineering, National University of Singapore, 117608, Singapore;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
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