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翅片管氟塑料换热器的流动传热特性

Flow and heat transfer characteristics of fin-tube fluoroplastics heat exchanger

  • 摘要: 为提升氟塑料换热器的流动传热性能,分析了翅片管氟塑料换热器的热阻占比,通过建立翅片管氟塑料换热器的流动传热模型,模拟研究了翅片参数、管间距和氟塑料种类对换热器流动传热性能的影响.结果表明:氟塑料换热器管外空气换热热阻和管壁导热热阻平均占比分别达到60.0%和30.0%以上;翅片厚度对努塞尔数(Nusselt number,Nu)和压降影响很小;当翅片间距和管纵向间距增大时,Nu增大,压降减小;当管横向间距减小时,Nu减小,压降增大;翅片间距、厚度、管横向和纵向间距分别为9、1.2、10和20 mm时,氟塑料换热器综合性能最好;与光管普通氟塑料换热器相比,计算工况内普通氟塑料和石墨烯氟塑料的翅片管换热器总传热系数分别提升2.5%~21.0%和16.0%~55.0%.

     

    Abstract: To improve the flow and heat transfer performance of fluoroplastics heat exchanger, the thermal resistance ratio of the fluoroplastics heat exchanger was analyzed. The flow and heat transfer model of fin-tube heat exchanger was established, and the effects of fin parameters, tube spacing parameters and fluoroplastics species on the flow and heat transfer performance of heat exchanger were simulated. The results show that the average thermal resistance ratios in air side and tube wall are up to 60.0% and 30.0%, respectively. Nusselt number(Nu)and pressure drop keep almost constant with the increasing of fin thickness. With the increasing of fin spacing and tube longitudinal spacing, Nu number is increased, and pressure drop is decreased. With the increasing of tube transverse spacing, Nu number is decreased, and pressure drop is increased. When fin spacing, thickness, tube transverse and longitudinal spacing are respective 9, 1.2, 10 and 20 mm, the optimal comprehensive performance of fluoroplastics heat exchanger can be obtained. Compared with heat exchanger with smooth fluoroplastics tube, the total heat transfer coefficients of the common fin-tube fluoroplastics heat exchanger and the fin-tube graphene flurorplastics heat exchanger are increased by 2.5%-21.0% and 16.0%-55.0%, respectively.

     

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