Effect of electrode arrangement on heat transfer enhancement by electrohydrodynamic conduction pumps in a rectangular channel

IF 6.1 2区 工程技术 Q2 ENERGY & FUELS
Yi-Bo Wang , He-Xiang Liu , Chen-Xi Wang , Ke-Chuan Yan , Shao-Yu Wang , Ben-Xi Zhang , Zheng Bo , Yan-Ru Yang , Xiao-Dong Wang
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Abstract

The present study investigates heat transfer enhancement by electrohydrodynamic (EHD) conduction pumps in a rectangular channel. The effect of electrode arrangement on flow and thermal performance of the rectangular channel by EHD conduction pumps are quantitatively discussed in terms of pressure drop and Nusselt number. The inlet laminar flow with Reynolds number ranging from 100 to 1000. The innovative point of this paper is validating the optimal electrode arrangement over a wider range of Reynolds numbers, the other one is investigating the impact of the number of electrodes on the heat transfer of the EHD conduction pump. The results show that compared to the arrangement of electrode pairs along the same side, electrode pairs arranged on the opposite side have a higher heat transfer capacity due to the stronger vortex strength and lower vortex temperature. For the above two arrangement methods, the heat transfer capacity can be significantly improved when the length of the high-voltage electrode is greater than that of the low-voltage electrode. This result is mainly due to the fact that the electric force enhances the vortex strength, which promotes the perturbation of the thermal boundary layer. The effect of the number of electrode pairs r on the heat transfer capacity is not monotonic. When r < 6, the heat transfer capacity increases with the increase of r due to the generation of more vortices. However, r > 6, as the number of electrode pairs increases, the heat transfer capacity decreases. This result is mainly due to the decrease in the area of the vortex and the increase in the temperature of the vortex.
电极排列对矩形通道中电动流体动力传导泵传热效果的影响
本研究探讨了电流体动力(EHD)传导泵在矩形通道中增强传热的问题。通过压降和努塞尔特数定量讨论了电极布置对 EHD 传导泵在矩形通道中的流动和热性能的影响。入口层流的雷诺数范围为 100 到 1000。本文的创新点在于验证了在更大雷诺数范围内的最佳电极布置,另一个创新点在于研究了电极数量对 EHD 传导泵传热的影响。结果表明,与沿同侧布置电极对相比,布置在对侧的电极对由于具有更强的涡流强度和更低的涡流温度而具有更高的传热能力。在上述两种排列方法中,当高压电极的长度大于低压电极的长度时,传热能力会显著提高。这一结果主要是由于电场力增强了涡流强度,从而促进了热边界层的扰动。电极对数 r 对传热能力的影响不是单调的。当 r < 6 时,由于产生更多的涡流,传热能力随 r 的增加而增加。然而,当 r > 6 时,随着电极对数量的增加,传热能力下降。造成这一结果的主要原因是漩涡面积减小和漩涡温度升高。
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来源期刊
Applied Thermal Engineering
Applied Thermal Engineering 工程技术-工程:机械
CiteScore
11.30
自引率
15.60%
发文量
1474
审稿时长
57 days
期刊介绍: Applied Thermal Engineering disseminates novel research related to the design, development and demonstration of components, devices, equipment, technologies and systems involving thermal processes for the production, storage, utilization and conservation of energy, with a focus on engineering application. The journal publishes high-quality and high-impact Original Research Articles, Review Articles, Short Communications and Letters to the Editor on cutting-edge innovations in research, and recent advances or issues of interest to the thermal engineering community.
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