Experimental study of heat transfer performance of porous wall microchannels

被引:0
作者
Zeng L. [1 ]
Zheng G. [1 ]
Deng D. [1 ]
Sun J. [1 ]
Liu Y. [1 ]
机构
[1] School of Mechanical Engineering and Automation, Harbin Institute of Technology (Shenzhen), Guangdong, Shenzhen
来源
Huagong Jinzhan/Chemical Industry and Engineering Progress | 2022年 / 41卷 / 09期
关键词
heat transfer; laser direct writing; microchannel; porous structure; two-phase flow;
D O I
10.16085/j.issn.1000-6613.2021-2258
中图分类号
学科分类号
摘要
As an efficient heat dissipation device, microchannel heat sinks have been widely used to solve the problem of high heat flux dissipation in micro-electronic devices, photoelectricity, automotive, aerospace industries and energy field and so on. To solve the problems of small heat transfer area, low heat transfer performance and boiling hysteresis of traditional smooth microchannels, a porous wall microchannel structure was proposed in this paper, and laser direct writing method was used to prepare efficient and stable porous wall microchannels. The porous wall microchannel significantly increases the heat transfer area, promotes the disturbance of the fluid, and provides many stable boiling cores, thereby enhancing single-phase and two-phase heat transfer. By building a microchannel heat transfer performance test system, the single-phase and two-phase heat transfer performance of porous wall microchannels and smooth microchannels were tested and compared. Experimental results indicated that the Nu number of porous wall microchannel was increased by 21%—31% compared with the untreated rectangular microchannel. In two-phase boiling heat transfer, porous structure promoted the nucleation of boiling bubbles and reduced the onset temperature of nucleate boiling (ONB), which was 35% lower than that of the untreated rectangular microchannel. At the same time, porous structure could ensure continuous liquid supply during the boiling process, thereby greatly improving the boiling heat transfer performance and avoiding the occurrence of drying out in advance. The two-phase boiling heat transfer coefficient htp was up to 83% higher than that of the untreated rectangular microchannel. The two-phase heat transfer coefficient htp of porous wall microchannel structure at the mass flux of G=500kg/(m2·s) was increased by 30% compared with that at the mass flux of G=200kg/(m2·s). © 2022 Chemical Industry Press. All rights reserved.
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页码:4625 / 4634
页数:9
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