曲线波纹振幅对带涡产生器管翅换热器换热性能影响研究

Study on the Influence of Curved Corrugation Amplitude on Heat Transfer Performance of Tube Fin Heat Exchanger with Vortex Generators

  • 摘要: 经研究发现,一种纵向曲线波纹与涡产生器组合的管翅式换热器翅片结构可以提高圆管管翅式换热器的换热性能。数值研究了曲线波纹振幅对换热器内流动与换热性能的影响,分析了不同振幅下通道内的涡量、换热、阻力和综合换热性能。研究结果发现,随着波纹振幅的增大,纵向涡的强度逐渐增强,流体对壁面的冲刷作用也相应增强,这有效破坏了热边界层,从而显著提升了换热器的换热性能。在Re=200~1 000范围内,与平直翅片和直波纹翅片相比,振幅为1.75 mm的纵向波纹翅片的Nu的最大增幅分别为72.7%和14.5%,f最大增加了161.8%和44.8%。所研究的纵向曲线波纹与涡产生器组合管翅式换热器的综合换热因子JF最大可达1.268,相较于平直翅片提高了26.8%。为便于工程应用,拟合了NufJF关于Re和波纹振幅h的关联式,NufJF偏差分别小于±3%、±10%和±6%。

     

    Abstract: Research has found that a fin structure combining longitudinal curved corrugations with vortex generators in a tube-fin heat exchanger can enhance the heat transfer performance of circular tube fin heat exchangers. The impact of amplitude of the curved longitudinal corrugation on fluid flow and heat transfer performance of a heat exchanger is investigated numerically. The vorticity field, heat transfer, resistance, and overall heat transfer performance are analyzed for different amplitudes. The results show that the intensity of longitudinal vortices gradually increases as the increase of amplitude. The fluid's scouring effect on the wall also intensifies with the increase of vortices, which effectively disrupts the thermal boundary layer and significantly improves the heat transfer performance of the exchanger. In the range of Re=200~1 000, compared with the plane fin and the straight corrugation fin, the maximum Nu for the longitudinal corrugated fin increases by 72.7% and 14.5%, respectively, while the friction factor f increases by 161.8% and 44.8%, respectively. The thermal performance factor JF for the curved corrugation can reach a maximum of 1.268, a 26.8% improvement over the plane fin. Correlations for Nu, f, and JF with deviations less than ±3%, ±10%, and ±6%, respectively, are fitted to facilitate their application in engineering.

     

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