分流板对大翅片间距管翅换热器流动传热特性的影响研究

Study on the Influence of Splitter Plate on Flow and Heat Transfer Characteristics of Tube-Fin Heat Exchangers with Large Fin Spacing

  • 摘要: 管翅式换热器因其结构简单、成本低廉,在工业领域得到了广泛应用。通常,提升换热性能往往伴随着流动阻力的增加。因此,在提高换热效率的同时降低流动阻力,对于换热器的优化设计具有重要意义。目前,关于分流板与管束组合的研究主要集中在横流管束换热器中,针对分流板与管翅式换热器结合的换热器的研究尚不充分。同时,翅片间距变化时,分流板对管翅式换热器综合性能影响的研究较少。因此,通过数值研究探讨了在翅片间距变化时分流板对换热器流动和传热特性的影响。研究结果表明,在圆管后加装分流板不仅能增大换热面积,提高换热器通道内的换热量,还能使流体流动更加均匀稳定,有效降低流动阻力,从而使综合强化传热评价因子显著提升。在雷诺数计算范围内,当翅片间距为30 mm,分流板长度为1.5倍圆管直径时,换热器通道内的换热量达到最大值,与未加装分流板的圆管相比增加了17.1%,同时阻力系数最大降低了7.4%,综合强化传热评价因子提高了19.8%。因此,加装分流板不仅能增大换热面积,还能降低通道内的流动阻力,从而有效提升换热器的综合换热能力,在实际工业生产中具有广泛的应用潜力。

     

    Abstract: Tube and fin heat exchangers are widely utilized in industrial applications due to their straightforward construction and cost-effectiveness. Typically, enhancements in heat transfer performance are accompanied by an increase in resistance loss. Hence, it is crucial to enhance heat transfer while simultaneously reducing flow resistance, which is essential for optimizing heat exchanger design. At present, the research on the combination of splitter plate and tube bundle mainly focuses on the cross-flow tube bundle heat exchanger, and the research on the heat exchanger for the combination of splitter plate and tube-fin heat exchanger is not yet sufficient. Meanwhile, when the fin spacing changes, there are fewer studies on the effect of fin spacing on the comprehensive performance of manifold in tube-fin heat exchanger with splitter plate. Therefore, in this paper, the effect of splitter plate on the flow and heat transfer characteristics of heat exchangers with different fin spacing is investigated numerically. The findings indicate that the addition of splitter plates behind the circular tube can increase the heat transfer area, thereby enhancing the heat transfer capacity within the heat exchanger channel. Additionally, it makes the fluid flow more uniform and stable, effectively reducing flow resistance, and significantly improving the integrated enhanced heat transfer evaluation factor. Within the studied range of Reynolds number, when the fin pitch is 30 mm and the splitter plate length is 1.5 times the tube diameter, the heat exchange capacity in the heat exchanger channel is maximized, showing a 17.1% increase compared to the round tube alone. The resistance coefficient is reduced by 7.4%, while the comprehensive enhanced heat transfer evaluation factor is improved by 19.8%. Consequently, the addition of splitter plates not only increases the heat transfer area but also streamlines the channel fluid flow, effectively enhancing the heat exchanger's overall heat transfer capacity and offering extensive application potential in actual industrial production.

     

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