Instability analysis of pressure drop and flow characteristics in mini-channel heat sink with phase-separated configuration

被引:2
|
作者
Li, Tengfei [1 ]
Luo, Xiaoping [1 ]
Li, Guizhong [1 ]
机构
[1] South China Univ Technol, Sch Mech & Automot Engn, Guangzhou 510641, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Flow instability; Counter-flow; Vapor/liquid separation structure; Minichannel; Pressure drop; BOILING INSTABILITIES; MICROCHANNEL; MEMBRANE;
D O I
10.1016/j.applthermaleng.2024.123755
中图分类号
O414.1 [热力学];
学科分类号
摘要
Improving flow boiling stability is crucial for ensuring the safety in fields such as thermal management and microfluidic technology. Based on vapor - liquid separation analysis, multiple -pore phase-separated configurations have been proven to effectively enhance the stability of flow boiling in mini-channels. However, these structures primarily focus on expelling vapor from the mini -channel outlet, and vapor - liquid separation between adjacent mini-channels has not been addressed. In order to enhance and quantitatively analyze the vapor - liquid separation effect of phase-separated configurations, three phase-separated configurations with porous permeable membranes are prepared and experimentally studied in counter-flow mini -channel heat sinks: multiple -pore phase-separated configuration, sparse-pore phase-separated configuration, and poreless phase-separated configuration. The study found that phase-separated configurations effectively achieve vapor - liquid separation between adjacent mini-channels, thereby improving vapor - liquid distribution within the channels. Compared to sparse-pore and poreless phase-separated configurations, the multiple -pore phase-separated configuration offers greater advantages in enhancing the flow stability of mini -channel systems. Among them, the multiple -pore phase-separated configuration shows a maximum reduction of 24.71 % in the two-phase flow pressure drop, and with the increase in heat flux, this reduction becomes more pronounced compared to the conventional poreless structure. Additionally, the vapor permeation parameter X for the multiple -pore phaseseparated configuration is increased by 27.66 % compared to the sparse-pore phase-separated structure, indicating a higher vapor transfer rate per unit time for the multiple -pore phase-separated structure. Simultaneously, the potential physical mechanisms underlying the suppression of flow instability in mini-channels by phaseseparated structures are discussed in this study.
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页数:18
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