详细信息

EXPERIMENTAL INVESTIGATION ON HEAT TRANSFER AND PRESSURE LOSS CHARACTERISTICS OF THE GROOVED HELICALLY COILED TUBE HEAT EXCHANGER  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:EXPERIMENTAL INVESTIGATION ON HEAT TRANSFER AND PRESSURE LOSS CHARACTERISTICS OF THE GROOVED HELICALLY COILED TUBE HEAT EXCHANGER

作者:Cao, Jiaming[1];Wang, Xuesheng[1];Yuan, Yuyang[1,2];Zhang, Zhao[1];Xiao, Zhengyan[1]

机构:[1]East China Univ Sci & Technol, Inst Chem Machinery, Shanghai, Peoples R China;[2]Trinity Coll Dublin, Dept Mech Mfg & Biomed Engn, Dublin, Ireland

年份:2024

卷号:55

期号:3

起止页码:75

外文期刊名:HEAT TRANSFER RESEARCH

收录:;EI(收录号:20240815594843);WOS:【SCI-EXPANDED(收录号:WOS:001116900400002)】;

语种:英文

外文关键词:helically coiled tube heat exchangers; effectiveness; heat transfer enhancement; flow resistance; experimental investigation

摘要:Helically coiled tube heat exchangers have long been a subject of intense research due to their compact structure and efficient heat transfer capabilities. To further augment their performance, this study proposes a grooved helically coiled tube heat exchanger and establishes an experimental platform for a comparative analysis against a conventional helically coiled tube heat exchanger. Through the utilization of water and steam as working fluids, a comprehensive series of experiments was conducted to investigate heat transfer and pressure drop characteristics. Applying the Wilson plot method, heat transfer coefficients were computed for both the tube and shell sides. The experimental results demonstrate that the maximum relative error of tube-side pressure drop in comparison with empirical correlations does not exceed 24%, while the average error for the tube-side heat transfer coefficient is approximately 13%. Moreover, heat transfer coefficients on the shell side can increase by up to 69%, albeit with a significant rise in pressure drop, reaching up to 96%. By employing heat exchanger effectiveness as a comprehensive criterion, the grooved helically coiled tube heat exchanger's effectiveness can increase by up to 23%. These outcomes suggest that the external grooves can effectively amplify the heat transfer efficiency of helically coiled tube heat exchangers.

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