Extensive Investigation of Hydrothermal Flow and Heat Performance Improvement in a 3D Tube Based on Varying Concavity Dimple and Corrugation Turbulator Configurations
{"title":"Extensive Investigation of Hydrothermal Flow and Heat Performance Improvement in a 3D Tube Based on Varying Concavity Dimple and Corrugation Turbulator Configurations","authors":"Saad Raad Al-Haidari, Ahmed Ramadhan Al-Obaidi","doi":"10.1002/htj.23346","DOIUrl":null,"url":null,"abstract":"<div>\n \n <p>This study explored the influence of geometric parameters on corrugated tube heat exchangers under turbulent flow conditions. Eighteen different configurations were evaluated using both numerical simulations and experimental methods. The simulations, ranging from Reynolds numbers of 4000 to 15,000, analyzed various tube diameters, shapes, and disturbances. Results demonstrated that dimpled tube configurations significantly enhanced heat transfer compared with smooth tubes. The best performance, a pressure drop efficiency of 1.41 at a Reynolds number of 4000, was achieved with 2-mm dimples spaced 20 mm apart in an in-line pattern. Validation of the numerical results against experimental data demonstrated a high level of accuracy. The maximum deviation for the Nusselt number was 12% in smooth tubes and 15% in dimpled tubes. The maximum deviation for the friction factor was 6.1% in smooth tubes and 8.3% in dimpled tubes. The numerical model accurately represented the full dimensions of a commercial heat exchanger. Grid independence tests were conducted using a three-dimensional unstructured. To ensure accurate results, the study used a tetrahedral mesh and a Realizable <i>k</i>–<i>ε</i> turbulence model in its simulations. The findings revealed that corrugated tubes with various ring and dimple configurations dramatically enhanced heat transfer. Specifically, tubes with diameter rings, distance between rings, dimpled-ring diameters, and distance between dimple rings achieved maximum enhancements of 45.5%, 35.009%, 67.95%, and 58.42%, respectively. Furthermore, dimpled tubes with different diameters and distances also outperformed smooth tubes, showing heat transfer increases of 42% and 38.8%. The optimized dimpled tube design offers a promising approach for improving heat exchanger performance while minimizing pressure drop. Future research can build upon these findings to further refine and optimize corrugated tube heat exchanger technology.</p>\n </div>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"54 5","pages":"3134-3162"},"PeriodicalIF":2.6000,"publicationDate":"2025-04-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Heat Transfer","FirstCategoryId":"1085","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/htj.23346","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"THERMODYNAMICS","Score":null,"Total":0}
引用次数: 0
Abstract
This study explored the influence of geometric parameters on corrugated tube heat exchangers under turbulent flow conditions. Eighteen different configurations were evaluated using both numerical simulations and experimental methods. The simulations, ranging from Reynolds numbers of 4000 to 15,000, analyzed various tube diameters, shapes, and disturbances. Results demonstrated that dimpled tube configurations significantly enhanced heat transfer compared with smooth tubes. The best performance, a pressure drop efficiency of 1.41 at a Reynolds number of 4000, was achieved with 2-mm dimples spaced 20 mm apart in an in-line pattern. Validation of the numerical results against experimental data demonstrated a high level of accuracy. The maximum deviation for the Nusselt number was 12% in smooth tubes and 15% in dimpled tubes. The maximum deviation for the friction factor was 6.1% in smooth tubes and 8.3% in dimpled tubes. The numerical model accurately represented the full dimensions of a commercial heat exchanger. Grid independence tests were conducted using a three-dimensional unstructured. To ensure accurate results, the study used a tetrahedral mesh and a Realizable k–ε turbulence model in its simulations. The findings revealed that corrugated tubes with various ring and dimple configurations dramatically enhanced heat transfer. Specifically, tubes with diameter rings, distance between rings, dimpled-ring diameters, and distance between dimple rings achieved maximum enhancements of 45.5%, 35.009%, 67.95%, and 58.42%, respectively. Furthermore, dimpled tubes with different diameters and distances also outperformed smooth tubes, showing heat transfer increases of 42% and 38.8%. The optimized dimpled tube design offers a promising approach for improving heat exchanger performance while minimizing pressure drop. Future research can build upon these findings to further refine and optimize corrugated tube heat exchanger technology.
研究了紊流条件下几何参数对波纹管换热器的影响。采用数值模拟和实验方法对18种不同的构型进行了评估。模拟的雷诺数从4000到15000不等,分析了不同的管径、形状和扰动。结果表明,与光滑管相比,凹陷管结构显著提高了换热性能。在雷诺数为4000时,当两毫米的凹槽以20毫米的间隔排列时,压降效率达到1.41。数值结果与实验数据的对比表明,数值结果具有较高的精度。努塞尔数的最大偏差在光滑管中为12%,在凹陷管中为15%。摩擦系数的最大偏差在光滑管中为6.1%,在凹陷管中为8.3%。该数值模型准确地反映了商用换热器的全部尺寸。网格独立性测试采用三维非结构化进行。为了保证结果的准确性,本研究采用了四面体网格和Realizable k -ε湍流模型进行模拟。结果表明,波纹管具有不同的环形和凹窝结构显著提高传热。其中,直径环、环间距离、凹陷环直径和凹陷环间距离的增强效果最大,分别为45.5%、35.009%、67.95%和58.42%。此外,不同直径和距离的凹槽管的换热性能也优于光滑管,分别提高了42%和38.8%。优化后的凹窝管设计为提高换热器性能同时减小压降提供了一种很有前途的方法。未来的研究可以建立在这些发现的基础上,进一步完善和优化波纹管换热器技术。