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Laminar Forced Convection and Heat Transfer Characteristics in a Square Channel Equipped with V-Wavy Surface

机译:配备V形表面的方通道中的层流强迫对流和传热特性。

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The numerical investigations on flow pattern and heat transfer characteristic in a heat exchanger channel equipped with V-wavy surface are examined. The influences of the flow attack angles (α = 15°, 20°, 25°, 30°, 35°, 40°, 45°, 50°, 55° and 60°) and wavy surface arrangements (V-tip pointing downstream called "V-Downstream", V-tip pointing upstream called "V-Upstream) are investigated for laminar regime, Re = 100-1200. The finite volume method with SIMPLE algorithm is used to solve the current research. The numerical result shows that the addition of the wavy surface in the heat exchanger channel can help to develop the heat transfer rate and thermal performance. The wavy surface generates the vortex flow through the test section that disturbs the thermal boundary layer on the heat transfer surface. The insertion of the wavy surface in the heating channel gives higher heat transfer rate around 1.5-10 times above the smooth channel depended on the flow attack angle, Reynolds number and wavy surface arrangement. In addition, the optimum thermal performance is around 3.0 at Re = 1200, α = 40° and V-Upstream.
机译:考察了带有V形波纹表面的换热器通道内流动模式和传热特性的数值研究。流动迎角(α= 15°,20°,25°,30°,35°,40°,45°,50°,55°和60°)和波浪形表面布置的影响(V型尖端指向下游研究了层流状态,Re = 100-1200,称为“ V-Downstream”,指向V-tip的上游称为“ V-Upstream”,采用SIMPLE算法的有限体积法解决了目前的研究,数值结果表明:在换热器通道中添加波浪形表面可以帮助提高传热速率和热性能,该波浪形表面会产生涡流流经测试段,从而扰乱传热表面上的热边界层。加热通道中的波浪形表面根据流动迎角,雷诺数和波浪形表面排列,提供比光滑通道高1.5-10倍的较高传热速率,此外,在Re = 1200,α时,最佳热性能约为3.0 = 40°和V上游。

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