Experimental study on the effect of hydraulic diameter on the flow boiling characteristics in microchannels

IF 5.8 2区 工程技术 Q1 ENGINEERING, MECHANICAL International Journal of Heat and Mass Transfer Pub Date : 2025-05-15 Epub Date: 2025-01-23 DOI:10.1016/j.ijheatmasstransfer.2025.126736
Zheng Zhang , Guanmin Zhang , Yi Zhang , Maocheng Tian
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Abstract

Microchannel flow boiling heat dissipation has emerged as an effective solution for managing high heat flux in electronic devices. The hydraulic diameter of microchannels plays a crucial role in influencing flow boiling characteristics and heat sink design, yet the relationship between hydraulic diameter and flow boiling remains inadequately explored. This study employs a visualization-based experimental system with six distinct channel diameters (250 μm -1500 μm) to examine the effects of hydraulic diameters on microchannel flow boiling heat transfer characteristics. In this study, the number of microchannels was three, the working fluid was deionized water, the heat flux ranged from 203 to 880 kW/m², the system outlet pressure was 101.325 kPa, the pressure drop ranged from 0.71099 to 18.021 kPa, and the vapor quality ranged from 0.00183 to 0.37536. Results indicate that variations in microchannel hydraulic diameters lead to significant changes in flow patterns, heat transfer coefficients, and pressure drops. At a hydraulic diameter of 250 μm, annular flow forms earlier but is more prone to dry out. The heat transfer coefficient increases progressively as the hydraulic diameter is reduced. When the heat transfer coefficient enters a relatively stable change, a hydraulic diameter of 1500 μm yields a heat transfer coefficient ranging from 15 to 30 kW/m²·K. Reducing the hydraulic diameter to 750 μm increases the heat transfer coefficient to a range of 40–60 kW/m²·K, while further reducing the hydraulic diameter to 250 μm elevates the heat transfer coefficient to between 65 and 90 kW/m²·K. Pressure drop is highly sensitive to hydraulic diameter, with channels under 500 μm exhibiting the highest values and more pronounced slope variations. The pressure drop decreases as the hydraulic diameter increases. Due to inertial forces, larger hydraulic diameters induce more significant fluctuations in pressure drop and wall temperature during backflow. Through Spearman correlation analysis, this study fits heat transfer and pressure drop friction coefficients adaptable to different hydraulic diameters. This work offers theoretical insights and practical design guidance for optimizing microchannel heat sinks.
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水力直径对微通道内流动沸腾特性影响的实验研究
微通道流动沸腾散热已成为控制电子器件高热流密度的有效解决方案。微通道的水力直径对流动沸腾特性和散热器设计有着至关重要的影响,但水力直径与流动沸腾之间的关系尚未得到充分的研究。本研究采用基于可视化的实验系统,采用六种不同的管道直径(250 μm -1500 μm)来研究水力直径对微通道流动沸腾换热特性的影响。在本研究中,微通道数为3个,工作流体为去离子水,热流密度为203 ~ 880 kW/m²,系统出口压力为101.325 kPa,压降为0.71099 ~ 18.021 kPa,蒸汽质量为0.00183 ~ 0.37536。结果表明,微通道水力直径的变化会导致流动模式、换热系数和压降的显著变化。水力直径为250 μm时,环空流动形成较早,但更容易发生干化。随着水力直径的减小,换热系数逐渐增大。当换热系数进入一个相对稳定的变化时,1500 μm的液力直径的换热系数在15 ~ 30 kW/m²·K之间。当液压直径减小到750 μm时,换热系数增加到40 ~ 60 kW/m²·K,而当液压直径进一步减小到250 μm时,换热系数增加到65 ~ 90 kW/m²·K。压降对水力直径高度敏感,在500 μm以下的通道中,压降值最高,坡度变化更明显。压降随液压直径的增大而减小。由于惯性力的作用,较大的水力直径在回流过程中会引起更大的压降和壁面温度波动。通过Spearman相关分析,拟合了不同水力直径下的换热系数和压降摩擦系数。这项工作为优化微通道散热器提供了理论见解和实际设计指导。
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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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