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Second-law analysis on plain fin-and-tube heat exchangers

机译:普通翅片管式换热器的第二定律分析

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Second-law analysis on the heat exchanger having plain fins on a staggered array of circular tubes was conducted on the basis of correlations of Nusselt number and friction factor proposed by Kim et al. (1998), from which the entropy generation rate was evaluated. Optimum Reynolds number and minimum entropy generation rate were found over different operating conditions. At a fixed heat duty, within the valid of range of Kim et al.'s correlation, the plain fin-and-tube heat exchanger should exhibit a small tube spacing in air flow direction, a large number of tube rows, and large fin thickness and the spacing between adjacent plain fins. There is an optimal ratio between tube spacing normal to air flow direction and the tube diameter. [References: 9]
机译:根据金等人提出的努塞尔数和摩擦系数的相关性,对在交错排列的圆管阵列上具有平片的热交换器进行了第二定律分析。 (1998),从中评估了熵的产生率。在不同的操作条件下,发现了最佳的雷诺数和最小的熵产生率。在固定的热负荷下,在Kim等人的相关关系的有效范围内,普通的翅片管式换热器在空气流动方向上应具有较小的管间距,大量的管排和较大的翅片厚度和相邻平鳍之间的间距。在垂直于气流方向的管间距和管直径之间存在最佳比例。 [参考:9]

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