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Thermal-hydraulic performance of fin-and-oval tube compact heat exchangers with innovative design of corrugated fin patterns

机译:翅片和卵形管紧凑型换热器的热工液压性能以及波纹状翅片的创新设计

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摘要

The flow field inside the heat exchangers is associated with maximum heat transfer, minimum pressure drop and smallest pumping power. During the recent decades, the developments in the application of longitudinal vortex generators as an effective technique and important research topic have increased the heat transfer enhancement in the design of compact heat exchangers. The main motivation of this research is to study thermal-hydraulic performance characteristics in a tube bank compact heat exchanger with introducing new design of fins and tube by using computational fluid dynamics approach. One-corrugated and three-corrugated fins with oval tubes are innovative design of the FTCHE (fin-and-tube compact heat exchanger) that promises a large leap in the development of minimized FTCHEs with increased thermal efficiency. The major advantage of such design is its ability to produce substantially increased thermal efficiency and performance criteria of FTCHE. The investigation of thermal-hydraulic performance criteria is conducted for Reynolds number in the range of 200-900. This study shows that the flow distinction between plain and corrugated fins has a profound influence on the thermal-hydrodynamic performance. The results reveal that the corrugated fins can considerably advance the thermal efficiency of the FTCHE with a moderate pressure loss penalty. The computational results indicate that the average Nusselt number for the FTCHE with corrugated fin can be increased up to 20.0% over the baseline case and the corresponding pressure difference decreased up to 19.0%. In addition, the results show that the average value of performance in one-corrugated and three-corrugated fins and oval tube compact heat exchangers up to 5% and 15% over the baseline case, respectively. The newly designed fin with oval tube shows potential improvement of heat transfer performance and moderate pressure loss in the FTCHE compared with the baseline case.
机译:热交换器内部的流场与最大的热传递,最小的压降和最小的泵送功率有关。在最近的几十年中,纵向涡流发生器作为一种有效技术和重要研究课题的应用发展,在紧凑型热交换器的设计中增加了传热的能力。这项研究的主要动机是通过使用计算流体动力学方法引入新的翅片和管设计,研究管束紧凑型换热器的热工水力特性。带有椭圆形管的单波纹和三波纹翅片是FTCHE(翅片和管紧凑型热交换器)的创新设计,它有望在最小化FTCHEs的开发和提高热效率方面取得重大飞跃。这种设计的主要优势在于其能够显着提高FTCHE的热效率和性能标准。对雷诺数在200-900范围内的热工液压性能标准进行了研究。这项研究表明,普通翅片和波纹翅片之间的流动区别对热流体动力学性能有深远的影响。结果表明,波纹状翅片可显着提高FTCHE的热效率,并具有适度的压力损失损失。计算结果表明,带波纹翅片的FTCHE的平均Nusselt值可以比基准情况下增加20.0%,而相应的压差则可以减少19.0%。此外,结果表明,单波纹翅片和三波纹翅片以及椭圆管紧凑型换热器的平均性能分别比基准情况高出5%和15%。与基线情况相比,新设计的带有椭圆形管的翅片显示了FTCHE中的传热性能和中等压力损失的潜在改善。

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