首页> 外文期刊>Numerical Heat Transfer, Part A. Application: An International Journal of Computation and Methodology >Numerical analysis of periodically developed fluid flow and heat transfer characteristics in the triangular wavy fin-and-tube heat exchanger based on field synergy principle
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Numerical analysis of periodically developed fluid flow and heat transfer characteristics in the triangular wavy fin-and-tube heat exchanger based on field synergy principle

机译:基于场协同原理的三角形波浪翅片管式换热器周期性发展的流体流动和传热特性的数值分析

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In this article the three-dimensional periodically developed incompressible flow in the triangular wavy fin-and-tube heat exchanger is numerically simulated. A novel CLEARER algorithm is adopted to guarantee the coupling between the pressure and velocity, and it can also overcome the severe grid non-orthogonality in the complex wavy fin-and-tube heat exchanger. The influence of wavy angle, fin pitch, tube diameter, and wavy density on pressure drop and heat transfer characteristics is provided under different Reynolds numbers. The numerical results show that with the increase of wavy angle, tube diameter, or wavy density both the friction factor and Colburn factor will increase, while the increase rate of friction factor is higher than that of the Colburn factor. Opposite to the wavy fin-and-tube heat exchanger with uniform inlet velocity distribution, the wavy fin-and-tube heat exchanger with periodically developed flow owns a higher Colburn factor at larger fin pitch. The influence of wavy angle, fin pitch, tube diameter, and wavy density on the heat transfer performance can all be explained well from the viewpoint of the field synergy principle, and it means that the higher Colburn factor can be attributed to the better synergy between the velocity field and temperature field. Those results may provide an insight into the heat transfer enhancement in the wavy fin-and-tube heat exchanger.
机译:在本文中,对三角形波浪形翅片管式换热器中的三维周期性发展的不可压缩流动进行了数值模拟。采用一种新颖的CLEARER算法来保证压力与速度之间的耦合,它还可以克服复杂的波浪形翅片管式换热器中严重的网格非正交性。在不同的雷诺数下,提供了波角,翅片节距,管径和波密度对压降和传热特性的影响。数值结果表明,随着波浪角,管径或波浪密度的增加,摩擦系数和科尔伯因数都会增加,而摩擦因数的增加率高于科尔伯因数。与具有均匀入口速度分布的波浪形翅片管式换热器相反,具有周期性发展流量的波浪形翅片管式换热器在较大的翅片节距处具有较高的科尔伯因数。从场协同原理的角度可以很好地解释波浪角,翅片节距,管径和波浪密度对传热性能的影响,这意味着较高的科尔伯因数可以归因于两者之间更好的协同作用。速度场和温度场。这些结果可以提供对波浪形翅片管式换热器中传热增强的了解。

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