Effects of Flow Pulsation and Surface Geometry On Heat Transfer Performance in a Channel with Teardrop-shaped Dimples Investigated by Large Eddy Simulation

0 ENGINEERING, MECHANICAL ASME journal of heat and mass transfer Pub Date : 2024-02-13 DOI:10.1115/1.4064735
K. Inokuma, Yuki Yawata, A. Murata, K. Iwamoto
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Abstract

Large eddy simulation was performed to investigate heat transfer performance of a pulsating flow over teardrop-shaped dimples. A total of six geometries of dimpled surfaces were examined for dimple arrangements of in-line/staggered/original and dimple inclination angle of 0-60 deg. Pulsating flows were generated by sinusoidally varying the volume-averaged velocity. The pulsation frequency and amplitude were changed for the Strouhal number of 0-0.60 and the root-mean-square velocity amplitude normalized by the bulk flow velocity of 0-0.14. The results showed that the surface-averaged Nusselt number and friction factor were larger for the pulsating flow case than those for the steady flow case. The surface-averaged Nusselt number ratio and the friction factor increased with the Strouhal number up to the Strouhal number of 0.30. For the Strouhal number larger than 0.30, they decreased with the Strouhal number or stayed almost constant. Consequently, the heat transfer efficiency index increased with the Strouhal number. The increase in the local Nusselt number ratio due to the flow pulsation was observed at the leading-edge region of the dimples. The results of the streamlines near the dimple showed that the swirling separation bubble was located closer to the leading-edge region due to the pulsation, which resulted in the increase of the absolute values of the turbulent heat flux and the local Nusselt number ratio.
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通过大涡流模拟研究流动脉动和表面几何形状对带有泪滴状凹坑的通道传热性能的影响
为研究水滴形凹点上脉动流的传热性能,进行了大涡流模拟。共研究了六种几何形状的凹陷表面,凹陷排列方式为内嵌式/交错式/原位式,凹陷倾角为 0-60 度。脉动流是通过正弦改变体积平均速度产生的。当斯特劳哈尔数为 0-0.60 时,脉动频率和脉动振幅发生变化;当速度的均方根振幅以 0-0.14 的体积流速度归一化时,脉动频率和振幅发生变化。结果表明,脉动流情况下的表面平均努塞尔特数和摩擦因数大于稳定流情况下的表面平均努塞尔特数和摩擦因数。表面平均努塞尔特数比和摩擦因数随着斯特劳哈尔数的增加而增加,直到斯特劳哈尔数达到 0.30。当斯特劳哈尔数大于 0.30 时,它们随着斯特劳哈尔数的增大而减小或几乎保持不变。因此,传热效率指数随斯特劳哈尔数的增加而增加。在凹窝的前缘区域观察到了由于流动脉动引起的局部努塞尔特数比的增加。酒窝附近的流线结果显示,由于脉动,漩涡分离气泡更靠近前缘区域,这导致了湍流热通量和局部努塞尔特数比绝对值的增加。
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