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Numerical study of secondary flows in curved ducts.

机译:弯管二次流的数值研究。

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摘要

The occurrence of secondary flow in curved ducts due to the centrifugal forces as well as wall temperature effects can often significantly influence the volume flux and heat transfer rates. In the present work, the secondary flow of an incompressible viscous fluid in a curved duct with and without sidewall heating is studied by using a finite volume method. It is known that for low Dean numbers, the secondary flow is characterized by a pair of counter-rotating vortices. The present study shows that as the Dean number is increased the secondary flow structure evolves into a double vortex pair for low aspect ratio ducts and roll-cells for ducts of high aspect ratio.;A stability diagram is obtained in the domain of curvature ratio and Reynolds number. It is found that for ducts of high curvature the onset of instability depends on the Dean number and the curvature ratio, while for ducts of small curvature the onset can be characterized by the Dean number alone. A comparison with the available theoretical and experimental results indicates good agreement. A correlation for the friction factor as a function of the Dean number and aspect ratio is developed. It is found to be in good agreement with the available experimental and computational results for a wide range of parameters.;When there is sidewall heating, the interaction between the centrifugal and the buoyancy forces characterizes the secondary flow structure. It is shown that as the Grashof number is increased, the friction factor can decrease due to the transition from centrifugally dominant flow to buoyancy dominated flow. It is also found that for curved ducts the inertial effect dominates and the heat transfer may be enhanced at lower Grashof numbers. In addition, over the range in which the computations were performed the curvature effect is shown to enhance the heat transfer rate.;Computations for turbulent flow were carried out using a non-linear two-equation turbulence model. The model is used to predict turbulent secondary flows in straight and curved ducts. Comparison with available experimental results indicates good agreement.
机译:由于离心力以及壁温的影响,弯曲管道中出现二次流动通常会显着影响体积通量和传热速率。在目前的工作中,通过使用有限体积法研究了带有和不带有侧壁加热的弯曲管道中不可压缩粘性流体的二次流动。众所周知,对于低Dean数,二次流的特征是一对反向旋转的涡流。本研究表明,随着Dean数的增加,对于低长宽比的风管,次级流动结构演变为双涡流对,对于高长宽比的风管,则形成了涡流室。;在曲率比和雷诺数。发现对于高曲率的导管,不稳定性的开始取决于迪安数和曲率比,而对于小曲率的导管,其发作仅可以由迪安数来表征。与可用的理论和实验结果进行比较表明吻合良好。建立了摩擦因数与迪恩数和纵横比的函数的相关性。它被发现与广泛参数的可用的实验和计算结果非常吻合。当有侧壁加热时,离心力和浮力之间的相互作用是二次流结构的特征。结果表明,随着Grashof数的增加,摩擦因数可能会由于从离心主导流向浮力主导流的过渡而减小。还发现,对于弯曲的管道,惯性效应起主导作用,并且在较低的格拉斯霍夫数下可以增强传热。此外,在执行计算的范围内,还显示出曲率效应以提高传热速率。使用非线性二方程湍流模型对湍流进行计算。该模型用于预测直管和弯管中的湍流二次流。与可用的实验结果进行比较表明吻合良好。

著录项

  • 作者

    Hur, Nahmkeon.;

  • 作者单位

    Stevens Institute of Technology.;

  • 授予单位 Stevens Institute of Technology.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 1988
  • 页码 165 p.
  • 总页数 165
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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