{"title":"Numerical simulation study on heat transfer enhancement by longitudinal fins attached to the outer surface of horizontal tubes in seawater distiller","authors":"Wen-Jing Xie , Hong-Cheng Pan , Zhi-Li Chen","doi":"10.1016/j.icheatmasstransfer.2025.108762","DOIUrl":null,"url":null,"abstract":"<div><div>Tubular distillation desalination is one of the most promising thermal desalination methods. The addition of fins outside the tube can improve the heat transfer performance of the desalination units. This paper focuses on optimizing the design of structural parameters of the fin outside the tube of tubular desalination is optimized by numerical simulation. The results indicate that: The overall heat transfer coefficient is most significantly influenced by fin quantity, followed by fin height, with input temperature having the least impact. The overall heat transfer coefficient initially increases and then decreases with rising fin quantity, peaking at 5–7 fins for optimal performance. Enhancing fin height improves heat transfer, but excessive height induces air vortices between fins, which diminish the enhancement effect. The optimal fin height is determined as 15 mm when paired with 5–7 fins. This study elucidates the heat transfer mechanisms of fin structures under multi-parameter coupling effects, providing theoretical foundations and parameter optimization strategies for the efficient design of desalination units.</div></div>","PeriodicalId":332,"journal":{"name":"International Communications in Heat and Mass Transfer","volume":"164 ","pages":"Article 108762"},"PeriodicalIF":6.4000,"publicationDate":"2025-03-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Communications in Heat and Mass Transfer","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0735193325001873","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"MECHANICS","Score":null,"Total":0}
引用次数: 0
Abstract
Tubular distillation desalination is one of the most promising thermal desalination methods. The addition of fins outside the tube can improve the heat transfer performance of the desalination units. This paper focuses on optimizing the design of structural parameters of the fin outside the tube of tubular desalination is optimized by numerical simulation. The results indicate that: The overall heat transfer coefficient is most significantly influenced by fin quantity, followed by fin height, with input temperature having the least impact. The overall heat transfer coefficient initially increases and then decreases with rising fin quantity, peaking at 5–7 fins for optimal performance. Enhancing fin height improves heat transfer, but excessive height induces air vortices between fins, which diminish the enhancement effect. The optimal fin height is determined as 15 mm when paired with 5–7 fins. This study elucidates the heat transfer mechanisms of fin structures under multi-parameter coupling effects, providing theoretical foundations and parameter optimization strategies for the efficient design of desalination units.
期刊介绍:
International Communications in Heat and Mass Transfer serves as a world forum for the rapid dissemination of new ideas, new measurement techniques, preliminary findings of ongoing investigations, discussions, and criticisms in the field of heat and mass transfer. Two types of manuscript will be considered for publication: communications (short reports of new work or discussions of work which has already been published) and summaries (abstracts of reports, theses or manuscripts which are too long for publication in full). Together with its companion publication, International Journal of Heat and Mass Transfer, with which it shares the same Board of Editors, this journal is read by research workers and engineers throughout the world.