Numerical and experimental investigation on condensing heat transfer and flow characteristics outside horizontal dentate-fin tubes

被引:4
|
作者
Li, Meng [1 ,2 ]
Tao, Leren [1 ,2 ]
Huang, Lihao [1 ,2 ]
Jin, Cheng [1 ,2 ]
机构
[1] Univ Shanghai Sci & Technol, Inst Refrigerat & Cryogen, Shanghai 200093, Peoples R China
[2] Univ Shanghai Sci & Technol, Shanghai Key Lab Multiphase Flow & Heat Transfer P, Shanghai 200093, Peoples R China
关键词
Dentate -fin tube; Fin density; Condensing heat transfer; Volume of fluid method; CFD; SURFACE CONDENSATION; VERTICAL TUBE; SIMULATION; SINGLE; MODEL; R134A; DYNAMICS; VOLUME; PLAIN; WATER;
D O I
10.1016/j.ijheatmasstransfer.2023.124403
中图分类号
O414.1 [热力学];
学科分类号
摘要
The condensing flow and heat-transfer characteristics around dentate-fin tubes were investigated using numerical and experimental methods. Using the examined computational model, the film flow characteristics and condensing heat-transfer coefficient of the dentate-fin tubes in the circumferential and axial directions were analyzed. Comprehensive information regarding the condensation process in high-performance tubes is provided for the first time. The results showed that the circumferential and axial film thicknesses of the dentate-fin tubes increased with increasing fin density. The liquid film distribution of dentate-fin tubes with a low fin density was relatively uniform, and condensate drainage was easy. The special heat-transfer structure of dentate-fin tubes was examined, and it was found that the complex heat-transfer structure led to variations in the surface tension, which changes the liquid-film distribution. The local condensing heat-transfer coefficient of the dentate-fin tubes was very sensitive to the liquid-film distribution. The optimal fin density corresponding to the maximum overall heat-transfer coefficient was obtained, which showed that the mechanism of heat-transfer enhancement for dentate-fin tubes was a joint effect of the heat-transfer area and liquid-film thickness.
引用
收藏
页数:17
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