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Heat transfer and pressure drop performance of twisted oval tube heat exchanger

机译:扭曲椭圆管式换热器的传热和降压性能

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Twisted oval tube heat exchanger is a type of heat exchanger that aims at improving the heat transfer coefficient of the tube side and also decreasing the pressure drop of the shell side. In the present work, tube side and shell side heat transfer and pressure drop performances of a twisted oval tube heat exchanger has been experimentally studied. The tube side study shows that the tube side heat transfer coefficient and pressure drop in a twisted oval tube are both higher than in a smooth round tube. The shell side study shows that the lower the modified Froude number Fr_M, the higher the shell side heat transfer coefficient and pressure drop. In order to comparatively analyze its shell side performance of the heat exchanger, a rod baffle heat exchanger with similar size of the twisted oval tube heat exchanger is designed and its performance is calculated with Gentry's method. The comparative study shows that the heat transfer coefficient of the twisted oval tube heat exchanger is higher and the pressure drop is lower than the rod baffle heat exchanger. In order to evaluate the overall performance of the twisted oval tube heat exchanger, a performance evaluation criterion considering both the tube side and shell side performance of a heat exchanger is proposed and applied. The analyze of the overall performance of the twisted oval tube shows that the twisted oval tube heat exchangers works more effective at low tube side flow rate and high shell side flow rate.
机译:扭曲椭圆管式热交换器是一种热交换器,其目的在于提高管侧的传热系数并减小壳侧的压降。在目前的工作中,已经对扭曲的椭圆管式换热器的管侧和壳侧的传热和压降性能进行了实验研究。管侧研究表明,在扭曲的椭圆形管中,管侧的传热系数和压降均高于光滑的圆形管。壳侧研究表明,修正弗洛德数Fr_M越低,壳侧传热系数和压降越高。为了比较分析该换热器的壳侧性能,设计了一种尺寸与扭曲椭圆管换热器相似的棒形折流板换热器,并利用Gentry方法计算了其性能。对比研究表明,与椭圆形折流板式换热器相比,扭曲椭圆管式换热器的传热系数更高,压降更低。为了评估扭曲椭圆管式换热器的整体性能,提出并应用了同时考虑换热器的管侧和壳侧性能的性能评估标准。对扭曲的椭圆管的整体性能的分析表明,扭曲的椭圆管热交换器在低管侧流速和高壳侧流速下更有效。

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