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Compound Heat Transfer Enhancement of Wavy Fin-and-Tube Heat Exchangers through Boundary Layer Restarting and Swirled Flow

机译:通过边界层重新启动和旋转流动的复合热传递增强波浪翅片管热交换器

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摘要

This study performs a 3D turbulent flow numerical simulation to improve heat transfer characteristics of wavy fin-and-tube heat exchangers. A compound design encompassing louver, flat, and vortex generator onto wavy fins can significantly enhance the heat transfer performance of wavy fin-and-tube heat exchangers. Replacement of wavy fins around tubes with flat fins is not effective as far as the reduction of thermal resistance is concerned, although an appreciable pressure drop reduction can be achieved. Adding two louvers with a width of 8 mm to the flat portion can reduce thermal resistance up to 6% in comparison with the reference wavy fin. Increasing the louver number and width can further decrease the thermal resistance. Also, it is found that the optimum louver angle is equal to the wavy angle for offering the lowest thermal resistance. Therefore, compound geometry with three louvers, a width of 12 mm, and the louver angle being equal to wavy angle with waffle height to be the same as fin pitch of the reference wavy fin has the most reduction in thermal resistance of 16% for a pumping power of 0.001 W. Adding punching longitudinal vortex generators on this compound geometry can further decrease thermal resistance up to 18%.
机译:该研究执行3D湍流流量数值模拟,以改善波纹翅片管热交换器的传热特性。包含百叶窗,平板和涡流发生器的复合设计在波纹翅片上可以显着提高波浪翅片管热交换器的传热性能。尽管可以实现明显的压降减少,但是只要可以实现显着的压降,就没有扁平鳍片周围的带扁平鳍片的波纹翅片无效。与参考波翅片相比,将宽度为8mm的宽度为8mm的两个百叶窗可降低高达6%的热阻。增加百叶窗数和宽度可以进一步降低热阻。而且,发现最佳的百叶变度等于用于提供最低热阻的波浪角度。因此,具有三个百叶窗的化合物几何形状,宽度为12毫米,百叶窗角度等于与奶盖高度的波浪角度与参考波翅片的翅片间距相同,其热阻最小为16%泵送功率为0.001W。在该化合物几何形状上添加冲孔纵向涡流发生器可以进一步降低高达18%的热阻。

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