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Numerical Analysis on Fully Developed Laminar Forced Convective Heat Transfer in Circular Tube with Internal Longitudinal Fins

机译:内纵向翅片圆管内充分发展的层流强迫对流换热的数值分析

摘要

Fully developed laminar forced convective heat transfer in a circular tube with internal longitudinal fins is analyzed using the finite difference method, with the proviso that the flow is also fully developed. We adopt two kinds of thermal boundary conditions at the outer wall of the tube: constant wall temperatures and uniform heat fluxes. Extended Nusselt numbers based on the outer wall temperature are compared for the wide range of the geometrical parameters and the follwing results are summarized: (1) The equivalent diameter of the conduit affects the velocity profile of the fluid and the resulting flow pattern controls the heat transfer mechanism. (2) When the thermal conductivity ratio of the fluid to the tube material is small, the heat transfer augmentation by the fins is not effective. (3) When the thermal conductivity ratio of the fluid to the tube material lied in the order of 100, the effect of wall thickness on the heat transfer coefficient can be neglect. Furthermore when this ratio is greater than 500, the thermal resistance of the fin can be ignored in respect to the heat transfer.
机译:使用有限差分法分析了带有内部纵向翅片的圆形管中充分发展的层流强迫对流换热,条件是流动也得到充分发展。我们在管的外壁采用两种热边界条件:恒定的壁温和均匀的热通量。比较了基于外壁温度的扩展Nusselt数的各种几何参数,并总结了以下结果:(1)管道的等效直径影响流体的速度分布,并且所产生的流场控制热量转移机制。 (2)当流体与管材料的导热率较小时,通过翅片进行的传热增加无效。 (3)当流体与管材料的热导率之比为100左右时,可以忽略壁厚对传热系数的影响。此外,当该比率大于500时,就传热而言,鳍片的热阻可以忽略。

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