CHARACTERISTICS OF FLOW OVER A CIRCULAR CYLINDER AT Red=140,000

Hyun Sik Kim, Jungil Lee, Jooha Kim, Haecheon Choi
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In the near wake of circular cylinder, it is observed that a vortical structure distorted in spanwise direction and weak vortex shedding intermittently occurs, inducing relatively low drag and lift fluctuations. INTRODUCTION A circular cylinder is a representative bluff body, found in the structures such as wind generator, lamp post, etc. The flow over a circular cylinder at subcritical Reynolds number exhibits various flow phenomena including boundary layer, separation, shear layer evolution and vortex shedding in the wake. Therefore, there have been numerous studies to understand the flow over a circular cylinder experimentally and numerically. However, the experimental results from several researchers show non-negligible variations among themselves (Bearman, 1969; Achenbach and Heinecke, 1981; West and Apelt, 1982; Farell and Blessmann, 1983; Cantwell & Coles, 1983; Szepessy and Bearman, 1992). Furthermore, some attempts were also made to predict the flow around a circular cylinder using large eddy simulation (LES; Fröhlich et al., 1998; Breuer, 2000), but those studies only dealt with the effects of numerics such as grid system, resolution and subgrid-scale models and could not evaluate the prediction performance from numerical simulation due to the scatter in the experimental results. Therefore, in the present study, we investigate the flow over a circular cylinder at a subcritical Reynolds number (Red = 140,000) from both the experimental and numerical approaches. EXPERIMENTAL & COMPUTATIONAL DETAILS August 28 30, 2013 Poitiers, France WAK1A 2 Figure 1. Experimental set-up for (a) force and surface pressure measurements; (b) PIV measurement. Experimental setup The present experiment is conducted in a closed-type wind tunnel whose size of test section is 900 mm × 900 mm. The turbulence intensity is lower than 0.3% at the free-stream velocity of 20 m/s. Figure 1a shows the schematic diagram of the present experimental set-up for force and surface pressure measurements, consisting of a circular cylinder, end plate, load cell, pressure holes, scannivalve, and manometer. The cylinder is made of ABS resin with the diameter d = 70 mm. The aspect ratio of the cylinder is 11.4. Boundary-layer thickness on the tunnel-wall is about 25 mm at 20 m/s. The end plate, suggested by Stansby (1974), is installed with the distance 35 mm from the top and bottom of the test section to remove the effect of the boundary layer. The blockage ratio of present setup is 7.8%. Drag force on the cylinder is measured directly using two load cells installed at the both end of cylinder and averaged for 80 seconds. There are nine holes for pressure measurement in the spanwise direction. The distance between pressure holes is 70 mm and each hole is connected directly to the scannivalve with Teflon tube. The free-stream velocity varies from 20 to 55 m/s, corresponding to the Reynolds numbers based on the freeFigure 2. (a) Schemtaic diagram of the computational domain and boundary conditions; (b) typical mesh near circular cylinder. Every 4th grid is shown. stream velocity and the cylinder diameter, Red = 90,000 – 260,000. Figure 1b shows the schematic diagram for particle image velocimetry (PIV) measurement. The PIV system consists of a Nd:Yag laser of 120 mJ, a CCD camera of 2048 × 2048 pixels resolution and a delay generator. The velocity measurement is conducted in xy-plane at the center of the cylinder span. A 60 mm lens mounted on a digital camera is used to provide a field of view, whose size is 130 mm × 130 mm. Computational details In the present study, LES of the flow over a circular cylinder is conducted at Red = 140,000. The governing equations of an unsteady incompressible viscous flow for LES are the filtered continuity and Navier-Stokes equations. For the time integration, a fully implicit method based on the Crank-Nicolson method is used. For the spatial discretization, we use a hybrid scheme (Yun et al. 2006): a third-order QUICK scheme is used in laminar flow region before separation to prevent the dispersion error caused by the central difference scheme, and the second-order central difference scheme is used elsewhere. The no-slip boundary condition on the cylinder surface is realized by the immersed boundary method by Kim et al. (2001) in the Cartesian coordinate system. The subgridscale stress for LES is modelled using the dynamic global model (Park et al., 2006; Lee et al., 2010). Figure 2a shows the schematic diagram of computational domain, coordinate system and boundary conditions used in this study. The computational domain is -15≤x/d≤15, 25≤y/d≤25, and 0≤z/d≤π, where x, y, and z denote the streamwise, transve rse, and spanwise directions, respectiAugust 28 30, 2013 Poitiers, France WAK1A 3 Table 1. 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引用次数: 1

Abstract

In the present study, we conduct both numerical and experimental studies to investigate the characteristics of flow over a circular cylinder at Red = 140,000, where Red is the Reynolds number based on the cylinder diameter d and free-stream velocity. Large eddy simulation (LES) is conducted for numerical investigation, and direct force and particle image velocimetry (PIV) measurements are conducted for experimental investigation. The drag and base pressure coefficients from present numerical and experimental studies agree well with each other. The instantaneous flow over a circular cylinder exhibits various flow structures such as laminar separation at the cylinder surface, shear-layer after the separation, vivid small-scale vortices and vortex shedding in the wake. In the near wake of circular cylinder, it is observed that a vortical structure distorted in spanwise direction and weak vortex shedding intermittently occurs, inducing relatively low drag and lift fluctuations. INTRODUCTION A circular cylinder is a representative bluff body, found in the structures such as wind generator, lamp post, etc. The flow over a circular cylinder at subcritical Reynolds number exhibits various flow phenomena including boundary layer, separation, shear layer evolution and vortex shedding in the wake. Therefore, there have been numerous studies to understand the flow over a circular cylinder experimentally and numerically. However, the experimental results from several researchers show non-negligible variations among themselves (Bearman, 1969; Achenbach and Heinecke, 1981; West and Apelt, 1982; Farell and Blessmann, 1983; Cantwell & Coles, 1983; Szepessy and Bearman, 1992). Furthermore, some attempts were also made to predict the flow around a circular cylinder using large eddy simulation (LES; Fröhlich et al., 1998; Breuer, 2000), but those studies only dealt with the effects of numerics such as grid system, resolution and subgrid-scale models and could not evaluate the prediction performance from numerical simulation due to the scatter in the experimental results. Therefore, in the present study, we investigate the flow over a circular cylinder at a subcritical Reynolds number (Red = 140,000) from both the experimental and numerical approaches. EXPERIMENTAL & COMPUTATIONAL DETAILS August 28 30, 2013 Poitiers, France WAK1A 2 Figure 1. Experimental set-up for (a) force and surface pressure measurements; (b) PIV measurement. Experimental setup The present experiment is conducted in a closed-type wind tunnel whose size of test section is 900 mm × 900 mm. The turbulence intensity is lower than 0.3% at the free-stream velocity of 20 m/s. Figure 1a shows the schematic diagram of the present experimental set-up for force and surface pressure measurements, consisting of a circular cylinder, end plate, load cell, pressure holes, scannivalve, and manometer. The cylinder is made of ABS resin with the diameter d = 70 mm. The aspect ratio of the cylinder is 11.4. Boundary-layer thickness on the tunnel-wall is about 25 mm at 20 m/s. The end plate, suggested by Stansby (1974), is installed with the distance 35 mm from the top and bottom of the test section to remove the effect of the boundary layer. The blockage ratio of present setup is 7.8%. Drag force on the cylinder is measured directly using two load cells installed at the both end of cylinder and averaged for 80 seconds. There are nine holes for pressure measurement in the spanwise direction. The distance between pressure holes is 70 mm and each hole is connected directly to the scannivalve with Teflon tube. The free-stream velocity varies from 20 to 55 m/s, corresponding to the Reynolds numbers based on the freeFigure 2. (a) Schemtaic diagram of the computational domain and boundary conditions; (b) typical mesh near circular cylinder. Every 4th grid is shown. stream velocity and the cylinder diameter, Red = 90,000 – 260,000. Figure 1b shows the schematic diagram for particle image velocimetry (PIV) measurement. The PIV system consists of a Nd:Yag laser of 120 mJ, a CCD camera of 2048 × 2048 pixels resolution and a delay generator. The velocity measurement is conducted in xy-plane at the center of the cylinder span. A 60 mm lens mounted on a digital camera is used to provide a field of view, whose size is 130 mm × 130 mm. Computational details In the present study, LES of the flow over a circular cylinder is conducted at Red = 140,000. The governing equations of an unsteady incompressible viscous flow for LES are the filtered continuity and Navier-Stokes equations. For the time integration, a fully implicit method based on the Crank-Nicolson method is used. For the spatial discretization, we use a hybrid scheme (Yun et al. 2006): a third-order QUICK scheme is used in laminar flow region before separation to prevent the dispersion error caused by the central difference scheme, and the second-order central difference scheme is used elsewhere. The no-slip boundary condition on the cylinder surface is realized by the immersed boundary method by Kim et al. (2001) in the Cartesian coordinate system. The subgridscale stress for LES is modelled using the dynamic global model (Park et al., 2006; Lee et al., 2010). Figure 2a shows the schematic diagram of computational domain, coordinate system and boundary conditions used in this study. The computational domain is -15≤x/d≤15, 25≤y/d≤25, and 0≤z/d≤π, where x, y, and z denote the streamwise, transve rse, and spanwise directions, respectiAugust 28 30, 2013 Poitiers, France WAK1A 3 Table 1. Flow statistics at Red = 140,000.
在红色=140,000时圆柱上的流动特性
在本研究中,我们进行了数值和实验研究,以研究在Red = 140,000时圆柱上的流动特性,其中Red是基于圆柱体直径d和自由流速度的雷诺数。采用大涡模拟(LES)进行数值研究,采用直接力和粒子图像测速(PIV)进行实验研究。从目前的数值和实验研究中得到的阻力系数和基压系数吻合较好。圆柱瞬时流动表现出多种流动结构,如圆柱表面的层流分离、分离后的剪切层、生动的小尺度涡和尾迹中的旋涡脱落。在圆柱近尾迹处,观察到沿展向扭曲的涡结构,间歇性地发生弱涡脱落,产生较低的阻力和升力波动。圆柱是一种典型的钝体,常见于风力发电机、灯柱等结构中。亚临界雷诺数下的圆柱流动表现出边界层、分离、剪切层演化和尾迹涡脱落等多种流动现象。因此,人们对圆柱上的流动进行了大量的实验和数值研究。然而,几位研究人员的实验结果显示,它们之间存在不可忽略的差异(Bearman, 1969;Achenbach and Heinecke, 1981;West和Apelt, 1982;法雷尔和布莱斯曼,1983;Cantwell & Coles, 1983;Szepessy和Bearman, 1992)。此外,还尝试用大涡模拟(LES;Fröhlich等,1998;Breuer, 2000),但这些研究只涉及网格系统、分辨率和亚网格尺度模型等数值的影响,由于实验结果的分散,无法评价数值模拟的预测性能。因此,在本研究中,我们从实验和数值两方面研究了亚临界雷诺数(Red = 140,000)下圆柱的流动。实验与计算细节2013年8月28日至30日,法国普瓦捷WAK1A 2图1(a)力和表面压力测量的实验装置;(b) PIV测量。本实验在试验段尺寸为900 mm × 900 mm的封闭式风洞中进行。自由流速度为20 m/s时,湍流强度小于0.3%。图1a显示了目前用于力和表面压力测量的实验装置的示意图,包括一个圆柱体、端板、称重传感器、压力孔、扫描阀和压力计。筒体材质为ABS树脂,直径d = 70mm。圆柱体的纵横比为11.4。在20m /s速度下,隧道壁面边界层厚度约为25mm。Stansby(1974)建议将端板安装在距离试验段顶部和底部35mm的位置,以消除附面层的影响。现有装置堵塞率为7.8%。用安装在气缸两端的两个测力元件直接测量气缸上的拉力,平均80秒。沿展向有9个孔用于压力测量。压力孔之间的距离为70mm,每个孔用特氟龙管直接连接到扫描阀上。自由流速度在20 ~ 55 m/s之间变化,对应于基于freeFigure 2的雷诺数。(a)计算域和边界条件示意图;(b)近圆柱典型网格。每隔4个网格显示。流速度与气缸直径,红= 9万- 26万。图1b为粒子图像测速(PIV)测量原理图。PIV系统由120mj Nd:Yag激光器、2048 × 2048像素分辨率CCD摄像机和延时发生器组成。速度测量在圆柱跨度中心的x平面上进行。视场使用安装在数码相机上的60mm镜头,尺寸为130mm × 130mm。在本研究中,在Red = 140,000处进行了圆柱流动的LES。非定常不可压缩粘滞流的控制方程为滤波连续性方程和Navier-Stokes方程。对于时间积分,采用基于Crank-Nicolson方法的全隐式方法。对于空间离散化,我们采用混合格式(Yun et al. 2006):分离前层流区域采用三阶QUICK格式,防止中心差分格式造成色散误差,其他区域采用二阶中心差分格式。 柱体表面无滑移边界条件由Kim等(2001)在笛卡尔坐标系下采用浸入边界法实现。使用动态全球模型模拟LES的亚网格尺度应力(Park et al., 2006;Lee et al., 2010)。图2a为本研究使用的计算域、坐标系和边界条件示意图。计算域为-15≤x/d≤15,25≤y/d≤25,0≤z/d≤π,其中x、y、z分别为顺流方向、横向方向和跨向方向,分别为2013年8月28日30日,法国普瓦蒂埃在Red处的流量统计= 140,000。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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