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首页> 外文期刊>Journal of Engineering >Effect of Flow Attack Angle for V-Wavy Plate on Flow and Heat Transfer in a Square Channel Heat Exchanger
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Effect of Flow Attack Angle for V-Wavy Plate on Flow and Heat Transfer in a Square Channel Heat Exchanger

机译:V型波纹板的流动迎角对方通道热交换器中流动和传热的影响

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摘要

Effects of flow attack angles of the V-wavy plate on flow and heat transfer in a square channel heat exchanger are investigated numerically. The V-wavy plates with V-tips pointing downstream and upstream called V-Downstream and V-Upstream, respectively, are examined for the Reynolds number in the range of 3000–10,000. The finite volume method with SIMPLE algorithm is selected to solve the present problem. The numerical results are presented in terms of flow and heat transfer visualization. The thermal performance analysis is also concluded in the form of Nusselt number ratio (Nu/Nu0), friction factor ratio (/), and thermal enhancement factor (TEF). The numerical result shows that the wavy plate can induce the swirling flow through the test section for all cases. The swirling flow disturbs the thermal boundary layer on the channel wall which is the reason for heat transfer enhancement. In range studies, the heat transfer rate increases around 3–6.5 and 2.8–6 times above the smooth channel for V-Downstream and V-Upstream, respectively. The optimum TEF is found at = 20° and Re = 3000 to be around 2.09 for V-Upstream case.
机译:数值研究了V形波纹板的迎角对流动和传热的影响。检查V形波浪板,其V形尖端分别指向下游和上游,称为V下游和V上游,其雷诺数在3000–10,000范围内。选择采用SIMPLE算法的有限体积方法来解决该问题。数值结果以流动和传热可视化的形式表示。热性能分析还以努塞尔数比(Nu / Nu0),摩擦系数比(/)和热增强系数(TEF)的形式得出结论。数值结果表明,在所有情况下,波浪形板都能引起涡流通过测试段。旋流扰动了通道壁上的热边界层,这是传热增强的原因。在范围研究中,对于V下游和V上游,传热速率分别比平滑通道高出大约3–6.5和2.8–6倍。在V-Upstream情况下,最佳TEF在= 20°和Re = 3000时约为2.09。

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