{"title":"恒定施加热通量条件下水平基底上核池沸腾过程中气泡横向合并对气泡动力学和传热影响的数值研究","authors":"Atindra Krishnan, Vijay K. Dhir","doi":"10.1016/j.ijheatmasstransfer.2025.127063","DOIUrl":null,"url":null,"abstract":"<div><div>In the present work, three-dimensional numerical simulations are performed for nucleate pool boiling, with coupled transient conduction in the solid substrate, to study the effect of lateral merger of bubbles from two adjacent cavity sites on bubble dynamics and heat transfer, at boiling inception. Level set method is used to track the liquid-vapor interface, and finite-difference schemes are used to discretize the governing equations. The waiting time is determined as the time taken for the cavity site temperature to recover to the nucleation temperature after bubble departure. The present study is done for pool boiling of saturated water at atmospheric pressure on a 7 mm x 7 mm portion of a 1 mm thick horizontal stainless-steel substrate having two identical cavity sites. The spacing between the two cavity sites is parametrically varied. A uniform, time-invariant heat flux is imposed at the bottom of the substrate. The solution of the coupled transient conduction in the solid substrate shows that lateral bubble merger results in a significant variation in the waiting time and in turn the bubble departure frequency with cavity spacing. The vapor production rate and heat transfer coefficient, both averaged over one bubble cycle, for cases in which the two bubbles merge laterally are smaller than those in which the bubbles do not merge. The average heat transfer coefficient over one bubble cycle for the largest cavity spacing is 15 % higher than that for the smallest cavity spacing investigated in this work.</div></div>","PeriodicalId":336,"journal":{"name":"International Journal of Heat and Mass Transfer","volume":"247 ","pages":"Article 127063"},"PeriodicalIF":5.0000,"publicationDate":"2025-04-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Numerical study of influence of lateral bubble merger on bubble dynamics and heat transfer during nucleate pool boiling on a horizontal substrate under a constant imposed heat flux\",\"authors\":\"Atindra Krishnan, Vijay K. 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A uniform, time-invariant heat flux is imposed at the bottom of the substrate. The solution of the coupled transient conduction in the solid substrate shows that lateral bubble merger results in a significant variation in the waiting time and in turn the bubble departure frequency with cavity spacing. The vapor production rate and heat transfer coefficient, both averaged over one bubble cycle, for cases in which the two bubbles merge laterally are smaller than those in which the bubbles do not merge. The average heat transfer coefficient over one bubble cycle for the largest cavity spacing is 15 % higher than that for the smallest cavity spacing investigated in this work.</div></div>\",\"PeriodicalId\":336,\"journal\":{\"name\":\"International Journal of Heat and Mass Transfer\",\"volume\":\"247 \",\"pages\":\"Article 127063\"},\"PeriodicalIF\":5.0000,\"publicationDate\":\"2025-04-18\",\"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/S0017931025004041\",\"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}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Heat and Mass Transfer","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0017931025004041","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
摘要
本文采用三维数值模拟方法,对固体衬底中耦合瞬态传导的核池沸腾过程进行了数值模拟,研究了沸腾开始时两个相邻空腔的气泡横向合并对气泡动力学和传热的影响。采用水平集方法跟踪汽液界面,采用有限差分格式对控制方程进行离散化。等待时间确定为气泡离开后空洞位置温度恢复到成核温度所花费的时间。本研究是在具有两个相同空腔位置的1mm厚水平不锈钢衬底的7mm x 7mm部分上,在常压下对饱和水进行池沸。两个空腔之间的间距是参数变化的。在基材的底部施加均匀的、定常的热通量。固体衬底中耦合瞬态传导的解表明,侧向气泡合并导致等待时间和气泡离开频率随空腔间距的显著变化。在一个气泡周期内,两个气泡横向合并的情况下,蒸汽产生率和传热系数都小于两个气泡不合并的情况。最大空腔间距的平均换热系数比最小空腔间距的平均换热系数高15%。
Numerical study of influence of lateral bubble merger on bubble dynamics and heat transfer during nucleate pool boiling on a horizontal substrate under a constant imposed heat flux
In the present work, three-dimensional numerical simulations are performed for nucleate pool boiling, with coupled transient conduction in the solid substrate, to study the effect of lateral merger of bubbles from two adjacent cavity sites on bubble dynamics and heat transfer, at boiling inception. Level set method is used to track the liquid-vapor interface, and finite-difference schemes are used to discretize the governing equations. The waiting time is determined as the time taken for the cavity site temperature to recover to the nucleation temperature after bubble departure. The present study is done for pool boiling of saturated water at atmospheric pressure on a 7 mm x 7 mm portion of a 1 mm thick horizontal stainless-steel substrate having two identical cavity sites. The spacing between the two cavity sites is parametrically varied. A uniform, time-invariant heat flux is imposed at the bottom of the substrate. The solution of the coupled transient conduction in the solid substrate shows that lateral bubble merger results in a significant variation in the waiting time and in turn the bubble departure frequency with cavity spacing. The vapor production rate and heat transfer coefficient, both averaged over one bubble cycle, for cases in which the two bubbles merge laterally are smaller than those in which the bubbles do not merge. The average heat transfer coefficient over one bubble cycle for the largest cavity spacing is 15 % higher than that for the smallest cavity spacing investigated in this work.
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