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Flow and aerodynamic noise control of a circular cylinder by local blowing

Published online by Cambridge University Press:  08 February 2024

Reza Maryami
Affiliation:
Department of Mechanics and Aerospace Engineering, Southern University of Science and Technology, Shenzhen, Guangdong 518055, PR China
Elias J.G. Arcondoulis
Affiliation:
Department of Mechanics and Aerospace Engineering, Southern University of Science and Technology, Shenzhen, Guangdong 518055, PR ChinaSchool of Civil Aerospace and Design Engineering, University of Bristol, Bristol BS8 1TR, UK
Yu Liu*
Affiliation:
Department of Mechanics and Aerospace Engineering, Southern University of Science and Technology, Shenzhen, Guangdong 518055, PR ChinaGuangdong Provincial Key Laboratory of Turbulence Research and Applications, Southern University of Science and Technology, Shenzhen, Guangdong 518055, PR China
*
†Email address for correspondence: liuy@sustech.edu.cn

Abstract

In this experimental study, the impact of symmetric local blowing on suppressing the vortex-induced noise of a circular cylinder was investigated. A highly instrumented cylinder with pressure taps and a series of blowing chambers was used to inject air along the span (seven times the cylinder diameter) at circumferential angles $\theta _{b}={\pm }41^{\circ }$, ${\pm }90^{\circ }$ and ${\pm }131^{\circ }$ corresponding to the boundary layer, shear layers on the cylinder and separated shear layers, respectively. The investigation aimed to understand the noise reduction mechanism of local blowing by conducting near-field pressure and far-field noise measurements in synchronisation with flow field velocity measurements. Near-field pressure was measured around the circumference of the cylinder using a remote-sensing technique and planar particle image velocimetry was implemented to measure the velocity of the wake flow field at a diameter-based Reynolds number of $Re=7\times 10^{4}$. The results revealed that the interaction of the rolling up separated shear layers, under the influence of high-momentum fluid travelling from the free stream to the wake, induced significant vertical flow movement in the vortex-formation region. This movement led to strong alternating surface pressure fluctuations at the cylinder's shoulders, contributing to the scattering of noise. It was demonstrated that local blowing delayed vortex shedding for all cases, except at $\theta _{b}={\pm }90^{\circ }$, which elongated the shear layers and pushed the high-momentum transfer area farther downstream. The application of local blowing at $\theta _{b}={\pm }41^{\circ }$ was particularly effective in increasing the vortex formation size due to reduced entrainment of fluid-bearing vorticity.

Information

Type
JFM Papers
Copyright
© The Author(s), 2024. Published by Cambridge University Press
Figure 0

Figure 1.Schematic diagram depicting (a) the experimental set-up with a cylinder in the aeroacoustic wind tunnel and (b) the top view of the planar PIV configuration.

Figure 1

Figure 2.(a) Schematic of the cylinder design, (b) the $xy$-plane of the cylinder and (c) the sensing area on the cylinder equipped with pressure taps, ${P}_{i}$ ($i=1:20$), distributed around the circumference of the cylinder at midspan. Note that only pressure taps $P_{6}$ to $P_{14}$ are visible in this diagram. The peripheral locations of all 20 pressure taps are listed in table 2.

Figure 2

Figure 3.Static pressure, $p_{st}$, distribution along the half-span of the chamber normalised by the mean static pressure, $\bar {p}_{st}$, in the case of LB90.

Figure 3

Table 1.Blowing flow rate, $Q_{b}$, velocity ratio, $U_{b}/U_{\infty }$ and corresponding $C_{\mu }$ values calculated using (2.1).

Figure 4

Figure 4.Schematic of the remote-sensing set-up for (a) the full view of the cylinder and (b) assembly view of the remote-sensing holder.

Figure 5

Table 2.Peripheral positions of the pressure taps, ${P}_{i}$ ($i=1:20$), at $z/D=0$.

Figure 6

Figure 5.Acoustic PSD, $\varPhi _{pp}$, plotted against $St$ for various LB cases. The labels $f_{1}$, $f_{2}$ and $f_{3}$ representthe fundamental vortex shedding tone (first harmonic), second and third harmonics, respectively.

Figure 7

Figure 6.Near-field PSD, $\varPhi _{pp,s}$, at $\theta =0^{\circ }$, $41^{\!\circ }$, $90^{\circ }$, $131^{\!\circ }$ and $180^{\circ }$. The labels $f_{1}$, $f_{2}$ and $f_{3}$ represent the fundamental vortex shedding tone (first harmonic), second and third harmonics, respectively.

Figure 8

Figure 7.(a) Lift coefficient PSD, $\phi _{_{C_{_L}C_{_L}}}$, and (b) drag coefficient PSD, $\phi _{_{C_{_D}C_{_D}}}$, as a function of $St$. The labels $f_{1}$ and $f_{3}$ represent the odd harmonics, while $f_{2}$ and $f_{4}$ represent the even harmonics.

Figure 9

Figure 8.Normalised time-averaged $x$-and $y$-components of velocity, (a–d) $\bar {u}/U_{\infty }$ and (e–h) $\bar {v}/U_{\infty }$, respectively, superimposed by the time-averaged streamline. The solid red circle, square and triangle symbols represent the vortex core centre at $x\approx L_{vc}$, the end of the recirculation region at $x\approx L_{r}$ (saddle point) and the end of the vortex-formation region at $x\approx L_{f}$, respectively. The white contour region in $\bar {u}/U_{\infty }$ shows the flow acceleration area (FAA).

Figure 10

Figure 9.(a) Normalised time-averaged streamwise velocity, $\bar {u}/U_{\infty }$, and (b) the root-mean-square (r.m.s.) of the vertical velocity fluctuations, $v'_{{rms}}/U_{\infty }$, along the centreline ($\kern0.08em y/D=0$). The solid circle, square and triangle symbols represent $x\approx L_{vc}$, $L_{r}$ and $L_{f}$, respectively. The vertical dashed grey lines indicate the base of the cylinder at $x/D=0.5$.

Figure 11

Table 3.The vortex core length, $x\approx L_{vc}$, the length of the recirculation region, $x\approx L_{r}$, the length of the vortex-formation region, $x\approx L_{f}$, and maximum centreline velocity deficit, $\bar {u}_d/U_{\infty }$, for the baseline and LB cases. The results are extracted from figure 9.

Figure 12

Figure 10.Normalised time-averaged $x$- and $y$-components of velocity, (ai–vi) $\bar {u}/U_{\infty }$ and (bi–vi) $\bar {v}/U_{\infty }$, respectively. The selected stations correspond to $x\approx L_{vc}$, $L_{r}$ and $L_{f}$ of the baseline and LB cases as shown in figure 9.

Figure 13

Figure 11.Variation of the normalised wake width, $W/D$, with respect to $x/D$. Curves in this figure are fitted splines to the original data, and the vertical dashed grey line indicates the base of the cylinder at $x/D=0.5$. The wake centreline corresponds to $W/D=0$.

Figure 14

Figure 12.Shear layer trajectory from the bottom side of the cylinders. Contour plots represent the normalised time-averaged vorticity, $\omega ^{*}=\bar {\omega }_{z}D/U_{\infty }$, and grey dots depict regions where $\omega ^{*}\geq 0.75$. The square symbols indicate the end of the shear layer at $x\approx L_{s}$ and $y\approx W_{s}$. The curves in this figure are fitted splines to the original data.

Figure 15

Figure 13.(a–d) Normalised time-averaged $x$-component of Reynolds stress, $\overline {u'u'}/U^{2}_{\infty }$, (e–h) normalised time-averaged $y$-component of Reynolds stress, $\overline {v'v'}/U^{2}_{\infty }$ and (i–l) normalised time-averaged shear stress, $\overline {u'v'}/U^{2}_{\infty }$. For each case, the solid circle, square and triangle symbols represent $x\approx L_{vc}$, $L_{r}$ and $L_{f}$, respectively, (see figure 9).

Figure 16

Figure 14.(ai–vi) Normalised time-averaged $x$-component of Reynolds stress, $\overline {u'u'}/U^{2}_{\infty }$, (bi–vi) normalised time-averaged $y$-component of Reynolds stress, $\overline {v'v'}/U^{2}_{\infty }$ and (ci–vi) normalised time-averaged shear stress, $\overline {u'v'}/U^{2}_{\infty }$, at different $x$-locations corresponding to $x\approx L_{vc}$, $L_{r}$ and $L_{f}$ for the baseline and LB cases as shown in figure 9.

Figure 17

Figure 15.Normalised TKE, $\mathrm {TKE^{*}}$, for the baseline and LB cases. For each case, the solid circle, square and triangle symbols represent $x\approx L_{vc}$, $L_{r}$ and $L_{f}$, respectively (see figure 9).

Figure 18

Figure 16.Streamwise velocity PSD, $\varPhi _{uu}=10\log _{10}\,{\phi _{uu}}$. (a–e) Isosurface of $\varPhi _{uu}$ where transparency decreases with increasing $\varPhi _{uu}$ and ( f–i) the $\varPhi _{uu}$ values along $a$ ($\kern0.08em y/D=0$) and $b$ ($\kern0.08em y/D=0.5$) for stations A ($x/D=0.7$), B ($x/D=1$), C ($x/D=1.5$) and E ($x/D=2.5$).

Figure 19

Figure 17.Vertical velocity PSD, $\varPhi _{vv}=10\log _{10}\,{\phi _{vv}}$. (a–e) Isosurface of $\varPhi _{vv}$ where transparency decreases with increasing $\varPhi _{vv}$ and ( f–i) the $\varPhi _{vv}$ values along $a$ ($\kern0.08em y/D=0$) and $b$ ($\kern0.08em y/D=0.5$) for stations A ($x/D=0.7$), B ($x/D=1$), C ($x/D=1.5$), D ($x/D=2$) and E ($x/D=2.5$).

Figure 20

Figure 18.Coherence between the near-field pressure and far-field noise, $\gamma ^{2}_{pp_{_s}}$, in terms of $St$ for the pressure taps located at $\theta =0^{\circ }$, $41^{\circ }$, $90^{\circ }$, $131^{\circ }$ and $180^{\circ }$. The labels $f_{1}$ and $f_{2}$ represent the fundamental vortex shedding tone (first harmonic) and second harmonic, respectively.

Figure 21

Figure 19.Streamwise velocity to far-field noise coherence ($\gamma ^{2}_{up}$). (a) Isosurface of $\gamma ^{2}_{up}$ where transparency decreases with increasing $\gamma ^{2}_{up}$. (b–e) The values of $\gamma ^{2}_{up}$ recorded in the $xy$-plane and ( f–i) the values of $\gamma ^{2}_{up}$ along $a$ ($\kern0.08em y/D=0$) and $b$ ($\kern0.08em y/D=0.5$) for stations A ($x/D=0.7$), B ($x/D=1$), C ($x/D=1.5$) and E ($x/D=2.5$).

Figure 22

Figure 20.Vertical velocity to far-field noise coherence ($\gamma ^{2}_{vp}$). (a) Isosurface of $\gamma ^{2}_{vp}$ where transparency decreases with increasing $\gamma ^{2}_{vp}$. (b–e) The values of $\gamma ^{2}_{vp}$ recorded in the $xy$-plane and ( f–i) the values of $\gamma ^{2}_{vp}$ along $a$ ($\kern0.08em y/D=0$) and $b$ ($\kern0.08em y/D=0.5$) for stations A ($x/D=0.7$), B ($x/D=1$), C ($x/D=1.5$) and E ($x/D=2.5$).

Figure 23

Figure 21.Isosurface of coherence between the $x$-component of velocity and near-field pressure, $\gamma ^{2}_{up_{_s}}$, where transparency decreases with increasing $\gamma ^{2}_{up_{_s}}$: (a) baseline; (b) LB41; (c) LB90; (d) LB131.

Figure 24

Figure 22.Isosurface of coherence between the $y$-component of velocity and near-field pressure, $\gamma ^{2}_{vp_{_s}}$, where transparency decreases with increasing $\gamma ^{2}_{vp_{_s}}$: (a) baseline; (b) LB41; (c) LB90; (d) LB131.

Figure 25

Figure 23.(a) Energy fraction, $\lambda _{n}/\varSigma \lambda _{n}$, and (b) cumulative energy, $\varSigma ^{n}_{1}\lambda _{n}/\varSigma \lambda _{n}$, of the POD modes as a function of mode number, $n$, for the baseline and LB cases.

Figure 26

Figure 24.The PSD of the mode time coefficient, $\varPhi _{cc}=10\log _{10}\,{\phi _{cc}}$, as a function of $St$ and mode number ($n$). The labels $f_{1}$, $f_{2}$ and $f_{3}$ represent the first harmonic (fundamental vortex shedding tone), second and third harmonics, respectively.

Figure 27

Figure 25.Autocorrelation of near-field pressure at $\theta =90^{\circ }$, $R_{p_{_s}p_{_{s}}}$, and far-field pressure, $R_{pp}$, with respect to normalised time delay, $\tau ^{*}=\tau U_{\infty }/D$, depicted by lines with and without symbols, respectively. The subplots present the real part of the wavelet coefficient, ${\rm I\!R}(W)$, applied to the time coefficient of mode 1 ($c_{1}$).

Figure 28

Figure 26.Flow structures corresponding to the first three POD modes ($n=1$–3) of the $x$-component of the velocity fluctuations ($u'/U_{\infty }$): (a–d) $n=1$; (e–h) $n=2$; (i–l) $n=3$. The solid circle, square and triangle symbols represent $x\approx L_{vc}$, $L_{r}$ and $L_{f}$, respectively, for each case (see figure 9).

Figure 29

Figure 27.Flow structures corresponding to the first three POD modes ($n=1$–3) of the $y$-component of the velocity fluctuations ($v'/U_{\infty }$): (a–d) $n=1$; (e–h) $n=2$; (i–l) $n=3$. The solid circle, square and triangle symbols represent $x\approx L_{vc}$, $L_{r}$ and $L_{f}$, respectively, for each case (see figure 9).

Figure 30

Figure 28.(a) Time history of the first POD mode time coefficient, $c_{1}$, of the baseline, normalised using its corresponding eigenvalue, $\lambda _{1}$. The red square markers superimposed on the $c_{1}/\sqrt {2\lambda _{1}}$-curve correspond to the instances of two sets of consecutive vortex shedding. The instants are presented using the normalised time, $t^{*}=tU_{\infty }/D$, from $t_{0}^{*}$ to $t_{8}^{*}$. (b,d) Isosurface of normalised instantaneous vorticity, $\omega '^{*}=-0.7$, coloured by $\bar {u}/U_{\infty }$. The black dashed lines represent $x\approx L_{vc}$ and $L_{f}$, and the dashed grey lines illustrate the movement trajectory of the vortices within $a_{0}$–$a{_4}$ and $b_{0}$–$b{_4}$. (c) Flow fields of $\omega '^{*}$ for consecutive instants within $t_{1}^{*}$–$t_{7}^{*}$. The $x$-positions of the vortices at each instant of the first and second sets of shedding are denoted by $a_{0}$–$a{_4}$ and $b_{0}$–$b{_4}$, respectively. These positions are extracted from (c) and figure 9 or table 3.

Figure 31

Figure 29.Time history of the first POD mode time coefficient normalised by its eigenvalue, $c_{1}/\sqrt {2\lambda _{1}}$, and isosurface of $\omega '^{*}=-0.7$ coloured by $\bar {u}/U_{\infty }$. The red square markers superimposed on the $c_{1}/\sqrt {2\lambda _{1}}$-curve correspond to the instances of two sets of consecutive vortex shedding from $t_{1}^{*}$ to $t_{8}^{*}$. The $x$-positions of the vortices at each instant of the first and second shedding sets are denoted by $a_{1}$–$a{_4}$ and $b_{0}$–$b{_4}$, respectively. These positions are extracted from figure 9 or table 3. The black dashed lines represent $x\approx L_{vc}$ and $L_{f}$, and the dashed grey lines depict the movement trajectory of the vortices within $a_{1}$–$a{_4}$ and $b_{0}$–$b{_4}$. Here (a) LB41; (b) LB90; (c) LB131.

Figure 32

Figure 30.Flow fields of $\omega '^{*}$ at consecutive instants within $t_{1}^{*}$–$t_{4}^{*}$ extracted from the time history of the first POD mode time coefficient (see figure 29): (a–d) LB41; (e–h) LB90; (i–l) LB131.

Figure 33

Figure 31.Schematic diagram illustrating the key flow characteristics influenced by the LB cases.