工程微观结构、流形尺寸和空间取向对微通道流动沸腾力学的协同效应

IF 5.8 2区 工程技术 Q1 ENGINEERING, MECHANICAL
Hanyang Ye , Huanyu Zhao , Xuwen Wang , Leymus Yong Xiang Lum , Jin Yao Ho
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引用次数: 0

摘要

小通道流动沸腾是一种高效的热管理方法。开放的小通道,其特点是在流动通道上方增加了一个额外的歧管,表现出更小的压降和两相流动的不稳定性。然而,流形设计的选择往往没有系统的评估,其对不同空间取向下流动沸腾性能的影响尚不清楚。本研究探讨了表面形态、流形尺寸和空间取向对开放小通道流动沸腾的协同影响。在制冷剂质量流量(m˙)分别为0.005 kg/s和0.009 kg/s(对应质量通量G为27 ~ 187 kg/m2·s)和有效热流(qeff)为2.9 kW/m2 ~ 170 kW/m2的条件下,以水平、垂直向上和垂直向下三个空间方向向小通道入口供应7℃过冷液。研究结果表明,与传统的封闭平面小通道相比,增加流形尺寸和表面微结构的整合不仅显著提高了热压性能,在水平流动中增强因子(Φ)高达25,而且在垂直向上流动中延迟了干干的发生,出口蒸汽质量(xoutlet)为0.98。这些增强归因于即使在较低的质量通量(G = 27 kg/m2·s)下,更大的歧管结合冷却表面上增加的成核位置密度,也能抑制流动不稳定性。然而,在垂直向下流动中,增加流道尺寸加剧了流动的不均匀分布,增加了液膜破裂的可能性,导致临界热流密度(CHF)比封闭的小通道减少了约50%,其中在qeff = 149 kW/m2和xoutlet = 0.86时观察到严重的干化。相比之下,封闭小通道在不同的空间取向上表现出相对一致的沸腾特性,这主要是由于气泡爆炸生长效应的主导。总之,这项工作不仅成功地识别了表面形态、流形尺寸和空间取向对微通道流动沸腾特性的协同效应,而且为优化不同取向下的微通道热工性能提供了全面的指导。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Synergistic effects of engineered microstructures, manifold size and spatial orientation on flow boiling mechanics in minichannels
Flow boiling in minichannels is a highly effective thermal management approach. Open minichannels, characterized by an extra manifold above the flow channels, exhibit reduced pressure drop and two-phase flow instability. However, manifold designs are often selected without systematic evaluation, and their impact on flow boiling performance under different spatial orientations remain unclear. This study investigates the synergistic influences of surface morphology, manifold size, and spatial orientation on flow boiling in open minichannels. Experiments were conducted at the refrigerant mass flow rates (m˙) of 0.005 kg/s and 0.009 kg/s (corresponding to mass fluxes G of 27 to 187 kg/m2·s), and effective heat fluxes (qeff) of 2.9 kW/m2 to 170 kW/m2, by supplying 7 °C subcooled liquid to the minichannels inlet in three spatial orientations (horizontal, vertical upward, and vertical downward flow). Compared to conventional closed plain minichannels, our results show that increasing manifold size and the integration of surface microstructures not only significantly improves thermohydraulic performance, with enhancement factor (Φ) up to 25 in horizontal flow, but it also delays the occurrence of dryout in vertical upward flow to an outlet vapor quality (xoutlet) of 0.98. These enhancements are attributed to the suppression of flow instabilities even at a lower mass flux (G = 27 kg/m2·s) enabled by larger manifolds combining with increased nucleation site density on the cooling surface. In vertical downward flow, however, increasing manifold sizes exacerbates flow maldistribution and increases the possibility of liquid film rupture, resulting in about 50 % reduction in critical heat flux (CHF) as compared to the closed minichannels, where severe dryout was observed at qeff = 149 kW/m2 and xoutlet = 0.86. In contrast, closed minichannels exhibits relatively consistent boiling characteristics across different spatial orientations, due to the dominant bubble explosive growth effect. In all, this work not only successfully identifies the synergistic effect of surface morphology, manifold size, and spatial orientation on flow boiling characteristics of minichannels, but it also provides comprehensive guidelines for optimizing minichannel thermohydraulic performance in different orientations.
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来源期刊
CiteScore
10.30
自引率
13.50%
发文量
1319
审稿时长
41 days
期刊介绍: International Journal of Heat and Mass Transfer is the vehicle for the exchange of basic ideas in heat and mass transfer between research workers and engineers throughout the world. It focuses on both analytical and experimental research, with an emphasis on contributions which increase the basic understanding of transfer processes and their application to engineering problems. Topics include: -New methods of measuring and/or correlating transport-property data -Energy engineering -Environmental applications of heat and/or mass transfer
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