{"title":"Research on phase change of vertical annular falling film heat transfer in tube at high liquid film Reynolds number","authors":"Liang Wang","doi":"10.1016/j.ijheatmasstransfer.2025.127820","DOIUrl":null,"url":null,"abstract":"<div><div>The turbulent gas–liquid heat transfer process in inlet section of falling film heat transfer in tube is very severe. To research the effect of high Reynolds number (<em>Re<sub>l</sub></em>=1.81 × 10<sup>4</sup>∼4.23 × 10<sup>4</sup>) phase change heat transfer characteristics and mechanism of falling liquid film in the scrubbing cooling tube. Vertical falling film flow model of the scrubbing cooling tube is established. The influence of liquid film temperature, <em>Re<sub>l</sub></em> and gas phase temperature on gas–liquid two-phase phase change heat transfer effect is studied using User Defined Function (UDF) in FLUENT. The results show that outlet temperature of gas–liquid mixed fluid rises with the increase of the initial gas temperature, and the gas–liquid heat transfer effect is most intense at 0–0.1 m. When gas temperature is 673 K, the maximum heat transfer coefficient (HTC)is about 899 W/(m<sup>2</sup>·K).When liquid film inlet temperature rises, HTC decreases, and the maximum deviation between calculated data and experimental correlations is about 12.43 %. When the gas temperature is between 1173 K and 1573 K, the cross-sectional temperature and water vapor content inside the tube increase. The HTC between gas and liquid phases is directly proportional to the liquid film <em>Re<sub>l</sub></em> and the dimensionless temperature. The maximum deviation between the fitted curve value and the calculated value is 11 %, fitting degree <em>R</em><sup>2</sup> = 0.98.</div></div>","PeriodicalId":336,"journal":{"name":"International Journal of Heat and Mass Transfer","volume":"255 ","pages":"Article 127820"},"PeriodicalIF":5.8000,"publicationDate":"2025-09-13","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/S001793102501155X","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
The turbulent gas–liquid heat transfer process in inlet section of falling film heat transfer in tube is very severe. To research the effect of high Reynolds number (Rel=1.81 × 104∼4.23 × 104) phase change heat transfer characteristics and mechanism of falling liquid film in the scrubbing cooling tube. Vertical falling film flow model of the scrubbing cooling tube is established. The influence of liquid film temperature, Rel and gas phase temperature on gas–liquid two-phase phase change heat transfer effect is studied using User Defined Function (UDF) in FLUENT. The results show that outlet temperature of gas–liquid mixed fluid rises with the increase of the initial gas temperature, and the gas–liquid heat transfer effect is most intense at 0–0.1 m. When gas temperature is 673 K, the maximum heat transfer coefficient (HTC)is about 899 W/(m2·K).When liquid film inlet temperature rises, HTC decreases, and the maximum deviation between calculated data and experimental correlations is about 12.43 %. When the gas temperature is between 1173 K and 1573 K, the cross-sectional temperature and water vapor content inside the tube increase. The HTC between gas and liquid phases is directly proportional to the liquid film Rel and the dimensionless temperature. The maximum deviation between the fitted curve value and the calculated value is 11 %, fitting degree R2 = 0.98.
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