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三维管烟气换热器传热特性的实验及模拟研究
引用本文:莫逊,朱冬生,林成迪. 三维管烟气换热器传热特性的实验及模拟研究[J]. 过程工程学报, 2018, 18(1): 41-48. DOI: 10.12034/j.issn.1009-606X.217198
作者姓名:莫逊  朱冬生  林成迪
作者单位:1. 中国科学院广州能源研究所,广东 广州 510640;2. 大冶斯瑞尔换热器有限公司,湖北 大冶 435100; 3. 中国科学院可再生能源重点实验室,广东 广州 510640;4. 广东省新能源和可再生能源研究开发与应用重点实验室,广东 广州 510640
基金项目:高效传热与节能减排集成技术团队;高效紧凑式低低温节能空冷岛
摘    要:通过实验对三维管换热元件与传统H型鳍片管进行测试,研究其传热特性. 结果表明,三维管换热器的总换热系数是H型鳍片管换热器的2?3倍,采用错列布置换热管比顺列布置换热管的阻力大. 修正的气侧对流换热系数关联式更符合实际,计算结果比原式提高约26%,FLUENT软件能很好模拟三维管换热器的实际情况,模拟结果误差较小.

关 键 词:烟气换热器  三维管  总换热系数  对流换热系数  数值模拟  
收稿时间:2017-03-30

Experimental and Numerical Research on Heat Transfer Characteristics of Three-dimensional Flue Gas Heat Exchanger
Xun MO Dongsheng ZHU Chengdi LIN. Experimental and Numerical Research on Heat Transfer Characteristics of Three-dimensional Flue Gas Heat Exchanger[J]. Chinese Journal of Process Engineering, 2018, 18(1): 41-48. DOI: 10.12034/j.issn.1009-606X.217198
Authors:Xun MO Dongsheng ZHU Chengdi LIN
Affiliation:1. Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou, Guangdong 510640, China; 2. Daye Sreal Heat Exchanger Co., Ltd., Daye, Hubei 435100, China; 3. Key Laboratory of Renewable Energy, Chinese Academy of Sciences, Guangzhou, Guangdong 510640, China; 4. Guangdong Key Laboratory of New and Renewable Energy Research and Development, Guangzhou, Guangdong 510640, China
Abstract:A comprehensive and detailed test had been performed for three-dimensional tube exchange components and traditional H-type fin tube through a prototype to investigated their heat transfer characterization. The results showed that the total heat transfer coefficient of the three-dimensional tube heat exchanger is 2 to 3 times that of the H-type fin tube heat exchanger, and the resistance of the heat exchanger in staggered arrangement was bigger than that of in-line arrangement. Besides, the modified correlation of gas side convective heat transfer was more realistic, and the calculated result is about 26% higher than that of the original correlation. FLUENT software can simulate the actual situation of three-dimensional tube heat exchanger, and the simulation results error is relatively small.
Keywords:flue gas heat exchanger   three-dimensional tube   total heat transfer coefficient   convective heat transfer coefficient   numerical simulation  
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