{"title":"Experimental study on flow boiling heat transfer in novel zipper-shaped micro fin array","authors":"Lin Qiao, Poh-Seng Lee, Meiyue Yan","doi":"10.1016/j.ijheatmasstransfer.2025.127118","DOIUrl":null,"url":null,"abstract":"<div><div>With the enhanced thermal design power (TDP) of CPU and GPU chips, there has been an urgent demand in effective thermal management technologies. Flow boiling heat transfer in microchannels is garnering widespread attention due to its superior heat dissipation capacity in compact spaces. This paper investigated flow boiling heat transfer and pressure drop characteristics in zipper-shaped micro fins array (3O1T and 1O1T) composed of oblique and trapezoidal fins compared to straight fins (SC). The experiments employed deionized water as working fluid, with mass flux varying from 148 to 325 kg/m²s and effective heat flux densities varying from 2 to 89 W/cm². The results revealed local heat transfer coefficients were 1.7 to 2.9 times and 2.7 to 4.0 times higher in 3O1T and 1O1T configurations compared to SC at mass flux of 148 kg/m²s. Additionally, the wall superheat in 3O1T and 1O1T configurations decreased by 2.5 °C and 5 °C, respectively, compared to SC at heat flux of 80W/cm². Furthermore, inlet pressure instabilities decreased by 53.5 % and 64.1 % in 3O1T and 1O1T configurations compared to SC at high mass flux. This improvement was attributed to mitigation of the confinement effect on vapor bubbles and elimination of the flow reversal phenomenon. Visualization studies showed that the 1O1T configuration helped in the fragmentation and creation of bubbles during nucleate boiling. Due to the superior comprehensive performance of 1O1T, it was recommended as the optimal micro fin structure in this study.</div></div>","PeriodicalId":336,"journal":{"name":"International Journal of Heat and Mass Transfer","volume":"247 ","pages":"Article 127118"},"PeriodicalIF":5.0000,"publicationDate":"2025-04-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Heat and Mass Transfer","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0017931025004570","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, MECHANICAL","Score":null,"Total":0}
引用次数: 0
Abstract
With the enhanced thermal design power (TDP) of CPU and GPU chips, there has been an urgent demand in effective thermal management technologies. Flow boiling heat transfer in microchannels is garnering widespread attention due to its superior heat dissipation capacity in compact spaces. This paper investigated flow boiling heat transfer and pressure drop characteristics in zipper-shaped micro fins array (3O1T and 1O1T) composed of oblique and trapezoidal fins compared to straight fins (SC). The experiments employed deionized water as working fluid, with mass flux varying from 148 to 325 kg/m²s and effective heat flux densities varying from 2 to 89 W/cm². The results revealed local heat transfer coefficients were 1.7 to 2.9 times and 2.7 to 4.0 times higher in 3O1T and 1O1T configurations compared to SC at mass flux of 148 kg/m²s. Additionally, the wall superheat in 3O1T and 1O1T configurations decreased by 2.5 °C and 5 °C, respectively, compared to SC at heat flux of 80W/cm². Furthermore, inlet pressure instabilities decreased by 53.5 % and 64.1 % in 3O1T and 1O1T configurations compared to SC at high mass flux. This improvement was attributed to mitigation of the confinement effect on vapor bubbles and elimination of the flow reversal phenomenon. Visualization studies showed that the 1O1T configuration helped in the fragmentation and creation of bubbles during nucleate boiling. Due to the superior comprehensive performance of 1O1T, it was recommended as the optimal micro fin structure in this study.
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