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Nonlinear optimal suppression of vortex shedding from a circular cylinder

Published online by Cambridge University Press:  23 June 2015

X. Mao*
Affiliation:
School of Engineering and Computer Sciences, Durham University, Durham DH1 3LE, UK
H. M. Blackburn
Affiliation:
Department of Mechanical and Aerospace Engineering, Monash University, 3800, Australia
S. J. Sherwin
Affiliation:
Department of Aeronautics, Imperial College London, South Kensington SW7 2AZ, UK
*
†Email address for correspondence: maoxuerui@sina.com

Abstract

This study is focused on two- and three-dimensional incompressible flow past a circular cylinder for Reynolds number $\mathit{Re}\leqslant 1000$ . To gain insight into the mechanisms underlying the suppression of unsteadiness for this flow we determine the nonlinear optimal open-loop control driven by surface-normal wall transpiration. The spanwise-constant wall transpiration is allowed to oscillate in time, although steady forcing is determined to be most effective. At low levels of control cost, defined as the square integration of the control, the sensitivity of unsteadiness with respect to wall transpiration is a good approximation of the optimal control. The distribution of this sensitivity suggests that the optimal control at small magnitude is achieved by applying suction upstream of the upper and lower separation points and blowing at the trailing edge. At high levels of wall transpiration, the assumptions underlying the linearized sensitivity calculation become invalid since the base flow is eventually altered by the size of the control forcing. The large-magnitude optimal control is observed to spread downstream of the separation point and draw the shear layer separation towards the rear of the cylinder through suction, while blowing along the centreline eliminates the recirculation bubble in the wake. We further demonstrate that it is possible to completely suppress vortex shedding in two- and three-dimensional flow past a circular cylinder up to $\mathit{Re}=1000$ , accompanied by 70 % drag reduction when a nonlinear optimal control of moderate magnitude (with root-mean-square value 8 % of the free-stream velocity) is applied. This is confirmed through linearized stability analysis about the steady-state solution when the nonlinear optimal wall transpiration is applied. While continuously distributed wall transpiration is not physically realizable, the study highlights localized regions where discrete control strategies could be further developed. It also highlights the appropriate range of application of linear and nonlinear optimal control to this type of flow problem.

Information

Type
Papers
Copyright
© 2015 Cambridge University Press 
Figure 0

Figure 1.Spectral elements in the computational domain: (a) overall domain and (b) detail close to cylinder.

Figure 1

Table 1.Convergence of the unsteadiness $A$ and the gradient $\boldsymbol{{\rm\nabla}}_{\boldsymbol{u}_{\boldsymbol{n}}}\mathscr{L}$ with respect to spectral polynomial order $P$, time step ${\rm\Delta}t$ and time interval to save the base flow ${\rm\Delta}T$ at $\mathit{Re}=100$, ${\it\omega}=0$ and ${\it\tau}=80$. The control cost is $E=0.001$ and $E=0.1$ for the convergence tests of the unsteadiness and the gradient respectively.

Figure 2

Figure 2.Unsteadiness $A$ under control of the sensitivity at various values of ${\it\omega}$ at $\mathit{Re}=100$, ${\it\tau}=80$ and $E=10^{-7}$.

Figure 3

Figure 3.Distribution of the sensitivity of the normalized normal control on the surface of the cylinder at (a) ${\it\tau}=80$ and various Reynolds numbers and (b) $\mathit{Re}=100$ and various final times ${\it\tau}$. Here, ${\it\theta}=0$ is the front stagnation point and ${\it\theta}={\rm\pi}$ is the trailing edge.

Figure 4

Figure 4.Deviation of the nonlinear solutions from the sensitivity at ${\it\tau}=30$ and (a) $\mathit{Re}=100$ and (b) $\mathit{Re}=1000$.

Figure 5

Figure 5.Distribution of the nonlinear optimal controls at ${\it\tau}=30$, $E=0.05$ and various Reynolds numbers.

Figure 6

Figure 6.Optimally controlled unsteadiness $A(\boldsymbol{u})$ as a function of $E^{1/2}$, which measures the magnitude of the control.

Figure 7

Figure 7.Contours of spanwise vorticity for the controlled flow at $\mathit{Re}=100$, ${\it\tau}=30$ and $E=0.05$. Panels (a), (b), (c) and (d) correspond to times $t=0$, 10, 30 and 50 respectively. Dashed lines, light solid lines and thick solid lines represent negative spanwise vorticity, positive spanwise vorticity and zero streamwise velocity respectively. The contour levels for spanwise vorticity are $[-2,-1.2,-0.4,0.4,1.2,2]$.

Figure 8

Figure 8.Contours of spanwise vorticity under the nonlinear optimal control at (a) $(\mathit{Re},E)=(100,0.01)$, (b) $(\mathit{Re},E)=(100,0.02)$, (c) $(\mathit{Re},E)=(100,0.05)$, (d) $(\mathit{Re},E)=(200,0.05)$, (e) $(\mathit{Re},E)=(300,0.05)$ and (f) $(\mathit{Re},E)=(1000,0.05)$. The result is collected at $t={\it\tau}=30$. Dashed lines, light solid lines and thick solid lines represent negative spanwise vorticity, positive spanwise vorticity and zero streamwise velocity respectively. The contour levels for spanwise vorticity are $[-2,-1.2,-0.4,0.4,1.2,2]$.

Figure 9

Figure 9.Isosurfaces of spanwise vorticity −0.6 (blue) and 0.6 (red) of three-dimensional flow under nonlinear optimal control at $\mathit{Re}=200$, ${\it\tau}=30$ and time (a) $t=0$, (b) $t=10$, (c) $t=20$ and (d) $t=30$.

Figure 10

Figure 10.Asymptotic stability of the steady flow subjected to the nonlinear optimal control. Here, ${\it\sigma}$ denotes the maximum growth rate of the most unstable eigenmode at spanwise wavenumber ${\it\beta}$.

Figure 11

Figure 11.Schematic of the boundary layer attachment–redirection mechanism of the nonlinear control. Thick dashed lines and thick solid lines are contour lines for vorticity −3 and 3 at $\mathit{Re}=1000$ under nonlinear control with $E=0.05$ and $t={\it\tau}=30$. Dotted lines denote the nonlinear optimal control, while lines inside and outside the cylinder represent suction and blowing respectively, as indicated by the arrows.

Figure 12

Figure 12.Development of the drag coefficient $C_{d}$ at (a) $\mathit{Re}=100$ and various control costs, and (b) $E=0.05$ and various Reynolds numbers.