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Effect of thermal buoyancy on vortex shedding past a circular cylinder in cross-flow at low Reynolds numbers

机译:在低雷诺数下,热浮力对涡流在横流中通过圆柱体的涡流脱落的影响

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摘要

This paper demonstrates the vortex shedding process behind a heated cylinder in a cross-flow at low Reynolds numbers under the influence of thermal buoyancy. The simulations were performed using an SUPG-based finite element technique. The range of Reynolds numbers was chosen to be 10-45. The flow was steady in the absence of thermal buoyancy. The eddy length and the separation angle were computed for the steady separated flow in the above range of Reynolds numbers. The results were in agreement with those reported in the literature. The Nusselt number distribution around the heated cylinder was also computed in the above range of Reynolds numbers for forced convective flows. The results compared fairly well with available experimental results. The effect of superimposed thermal buoyancy in the same range of Reynolds numbers was studied for various Richardson numbers. The steady separated flows become unsteady periodic in the presence of superimposed thermal buoyancy. For the unsteady periodic flows, the Strouhal numbers were computed. The separation angles and average Nusselt number for such unsteady flows were found to vary with time.
机译:本文演示了在热浮力的影响下,在低雷诺数的横流中,加热圆柱体后部的涡流脱落过程。使用基于SUPG的有限元技术进行了仿真。雷诺数的范围选择为10-45。在没有热浮力的情况下,流量稳定。计算了以上雷诺数范围内稳定分离流的涡旋长度和分离角。结果与文献报道一致。在强制对流流动的雷诺数的上述范围内,还计算了加热圆柱​​体周围的Nusselt数分布。结果与可用的实验结果相当好。对于各种理查森数,研究了在相同雷诺数范围内叠加热浮力的影响。在存在叠加的热浮力的情况下,稳定的分离流变得不稳定。对于不稳定的周期性流动,计算了Strouhal数。发现这种不稳定流动的分离角和平均努塞尔数随时间变化。

著录项

  • 来源
    《International Journal of Heat and Mass Transfer》 |2009年第8期|1897-1912|共16页
  • 作者

    G. Biswas; Sandip Sarkar;

  • 作者单位

    Department of Mechanical Engineering, Indian Institute of Technology - Kanpur, Kanpur 208 016, India;

    Department of Mechanical Engineering, Indian Institute of Technology - Kanpur, Kanpur 208 016, India;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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