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Secondary vortex, laminar separation bubble and vortex shedding in flow past a low aspect ratio circular cylinder

Published online by Cambridge University Press:  08 November 2021

Gaurav Chopra
Affiliation:
Department of Aerospace Engineering, Indian Institute of Technology Kanpur, 208016 Kanpur, India
Sanjay Mittal*
Affiliation:
Department of Aerospace Engineering, Indian Institute of Technology Kanpur, 208016 Kanpur, India
*
†Email address for correspondence: smittal@iitk.ac.in

Abstract

Large eddy simulation of flow past a circular cylinder of low aspect ratio ($AR=1$ and $3$), spanning subcritical, critical and supercritical regimes, is carried out for $2\times 10^3 \le Re \le 4\times 10^5$. The end walls restrict three-dimensionality of the flow. The critical $Re$ for the onset of the critical regime is significantly lower for small aspect ratio cylinders. The evolution of secondary vortex (SV), laminar separation bubble (LSB) and the related transition of boundary layer with $Re$ is investigated. The plateau in the surface pressure due to LSB is modified by the presence of SV. Proper orthogonal decomposition of surface pressure reveals that although the vortex shedding mode is most dominant throughout the $Re$ regime studied, significant energy of the flow lies in a symmetric mode that corresponds to expansion–contraction of the vortex formation region and is responsible for bursts of weak vortex shedding. A triple decomposition of the time signals comprising of contributions from shear layer vortices, von Kármán vortex shedding and low frequency modulation due to the symmetric mode of flow is proposed. A moving average, with appropriate size of window, is utilized to estimate the component due to vortex shedding. It is used to assess the variation, with $Re$, of strength of vortex shedding as well as its coherence along the span. Weakening of vortex shedding in the high subcritical and critical regime is followed by its rejuvenation in the supercritical regime. Its spanwise correlation is high in the subcritical regime, decreases in the critical regime and improves again in the supercritical regime.

Information

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1. Flow past a circular cylinder: schematic of the computational domain and the boundary conditions.

Figure 1

Figure 2. Flow past a circular cylinder: two-dimensional section of finite element mesh in the $x$–$y$ plane; (a) full view and (b) close-up view near the cylinder.

Figure 2

Figure 3. The $Re=4.0\times 10^5$ flow past a cylinder of $L_z=1D$: surface distribution of (a) skin friction coefficient; (b) $y^+$ corresponding to the element height of the mesh on the surface of the cylinder for the time- and span-averaged flow.

Figure 3

Figure 4. The $L_z=1D$, $Re=4.0\times 10^4$ flow past a cylinder with and without end plates at the lateral boundaries: surface distribution of time- and span-averaged (a) coefficient of pressure ($\overline {C}_P$) and (b) skin friction ($\overline {C}_f$) for slip, no-slip conditions on the end plates and no-slip conditions on the end plates but excluding the sidewall boundary layer (BL) while span averaging. Shown in panel (c) is the spanwise variation of $\overline {C}_P$ at the shoulder ($\theta =90^{\circ }$) via broken line and base of the cylinder ($\theta =180^{\circ }$) via solid line. Streamlines for the time- and span-averaged are shown for (d) slip wall, (e) no-slip wall and (f) no-slip wall excluding the sidewall boundary layer while span averaging.

Figure 4

Table 1. Flow past a circular cylinder of $L_z=1D$ with and without end plates at the lateral boundaries: time-averaged coefficient of drag ($\overline {C}_D$); r.m.s. of coefficient of lift ($C_{Lrms}$) and non-dimensional vortex shedding frequency ($St$) at $Re=2.0\times 10^4$ and $4.0\times 10^4$. The abbreviation ‘S & B’ stands for Szepessy & Bearman (1992); BC denotes boundary condition.

Figure 5

Figure 5. Flow past a circular cylinder: variation of time-averaged coefficient of drag ($\overline {C}_D$) with Reynolds number. The abbreviations are: EP, cylinder with side end plates; S & B, Szepessy & Bearman (1992); S, Schewe (1983); A, Achenbach (1968); L, Lehmkuhl et al. (2014); C, Cheng et al. (2017); B, Bearman (1969) and D: Desai et al. (2020).

Figure 6

Figure 6. Flow past a circular cylinder: (a) the variation of time-averaged drag force $\overline {F}_x$ and $\overline {C}_D Re^2$ with $Re$ for the data from Schewe (1983) for cylinder with $L_z=10D$ and (b) the variation of time-averaged coefficient of drag ($\overline {C}_D$) and $\overline {C}_D Re^2$ with Reynolds number from present numerical simulations on cylinder with $L_z=1D$.

Figure 7

Figure 7. Flow past a circular cylinder: variation of r.m.s. of coefficient of (a) lift ($C_{Lrms}$) and (b) drag ($C_{Drms}$) with Reynolds number. The abbreviations are: EP, cylinder with end plates; S & B, Szepessy & Bearman (1992); K, Keefe (1962); F, Fung (1960); S, Schewe (1983); R, Rodríguez et al. (2015); D, Desai et al. (2020).

Figure 8

Figure 8. Flow past a $Re=0.5\times 10^5$ circular cylinder: (a–c) $\overline {ww}$ in the $x$–$z$ plane at $y/D=0.05$ and (d–f) span-averaged $\overline {u'u'}$ in the $x$–$y$ plane where panels (a,d) are for a cylinder with $L_z=1D$ and slip condition on lateral boundaries, panels (b,e) are for $L_z=1D$ and no-slip condition on the end plates and panels (c,f) are for $L_z=3D$ and with slip condition on lateral boundaries.

Figure 9

Figure 9. Flow past a circular cylinder with $L_z=1D$: time- and span-averaged streamlines for (a) $Re=0.02\times 10^5$, (b) $Re=0.2\times 10^5$, (c) $Re=0.4\times 10^5$, (d) $Re=1.4\times 10^5$, (e) $Re=3.0\times 10^5$, and (f) $Re=3.5\times 10^5$. The insets shows the close-up views of the flow to bring out the SV and LSB.

Figure 10

Figure 10. Flow past a circular cylinder with $L_z=1D$: the left-hand column of the figure shows the close-up view of the time- and span-averaged streamlines near the upper shoulder of the cylinder and the right-hand column shows the time- and span-averaged coefficient of pressure and skin friction distribution of the upper surface of cylinder ($0\leq \theta \leq 180$) for $Re=$ (a) $0.02\times 10^5$, (b) $0.2\times 10^5$, and (c) $4.0\times 10^5$. The close-up view of the upper shoulder to enlarge the SV and LSB for $Re=4.0\times 10^5$ is shown in panel (d). The LS, secondary attachment (SA), secondary separation (SS), turbulent attachment (TA) and turbulent separation (TS) points are also shown in the figure.

Figure 11

Figure 11. Flow past a circular cylinder with $L_z=1D$: schematic of time- and span-averaged streamlines to show various flows observed in present study. (a) Laminar separation of boundary layer without TA; neither SV nor LSB is observed. Panel (b) shows LS without TA; SV is observed downstream of LS. Panel (c) shows LS with TA; both SV and LSB are observed. Panel (d) shows the variation of time- and span-averaged LS, SA, SS, TA and TS points with $Re$. The regions of SV and LSB are shaded in purple and sky-black colours, respectively. The abbreviations are: C, Cheng et al. (2017); A, Achenbach (1968); S & H, Son & Hanratty (1969).

Figure 12

Figure 12. Flow past a circular cylinder with $L_z=1D$: (a) surface distribution of time- and span-averaged coefficient of pressure ($\overline {C}_P$) for various $Re$ and (b) variation of time- and span-averaged coefficient of peak suction pressure ($-\overline {C}_{Ppeak}$) and its location ($\theta _{C_{Ppeak}}$) with $Re$. The abbreviations are: P, present; T, Tani (1964); C, Cheng et al. (2017); S & B, Szepessy & Bearman (1992).

Figure 13

Figure 13. Flow past a circular cylinder: space–time variation of the coefficient of pressure ($C_P(\theta,t)$) on the surface of the cylinder (left) and time variation of $C_P(\theta =90^{\circ },t)$ (right) at midspan for $Re=$ (a) $0.6\times 10^5$, (b) $1.5\times 10^5$ and (c) $3.5\times 10^5$. Additionally, $\tilde {C}_P(\theta =90^{\circ },t)$ is shown in the line plots on the right.

Figure 14

Figure 14. The POD of moving and span-averaged surface pressure ($\tilde {C}_P(\theta,t)$) for $\mbox {{Re}}=0.6\times 10^5$: (a) the energy content of the first 10 modes; (b,c) the top two antisymmetric and symmetric modes, respectively.

Figure 15

Figure 15. POD of low-pass filtered span-averaged surface pressure ($\tilde {C}_P(\theta,t)$): (a) variation of percentage energy content of $AS_1$, $S_1$, $S_2$ and $AS_2$ modes with $\mbox {{Re}}$. Surface pressure distribution of eigenmodes corresponding to mode $AS_1$ (b) and $S_1$ (d) for various $\mbox {{Re}}$. Panels (c,e) show the close-up views of panels (b,d), respectively, to bring out the variations in $AS_1$ and $S_1$ modes due to SV and LSB at $Re=1.5\times 10^5$ and $3.5\times 10^5$. Here, LS, TA and TS correspond to the points of laminar separation, TA and turbulent separation, respectively. The variation within the SV is shown with a thicker line in panels (c,e).

Figure 16

Figure 16. Flow past a circular cylinder with $L_z=1D$: (a) variation, with $Re$, of r.m.s. of $C_P$ ($=C_{Prms}$) averaged on the two shoulders ($\theta =\pm 90^{\circ }$) of the cylinder and r.m.s. of $C_L$ ($C_{Lrms}$). Shown in panel (b) is the variation of the vortex formation length ($L_f$) with $Re$. The abbreviations are: P, present; S & B, Szepessy & Bearman (1992); B, Bloor (1964); D, Desai et al. (2020).

Figure 17

Figure 17. Flow past a circular cylinder: variation of non-dimensional vortex shedding frequency, Strouhal number ($St$), with Reynolds number. The abbreviations are: S & B, Szepessy & Bearman (1992); R, Rodríguez et al. (2015); S, Schewe (1983); B, Bearman (1969).

Figure 18

Figure 18. Flow past a circular cylinder: space–time plot of coefficient of pressure ($C_{P}(\theta =90^{\circ },t,z)$) (a,d,g), moving averaged coefficient of pressure ($\tilde {C}_{P}(\theta =90^{\circ },t,z)$) (b,e,h) and fluctuations associated with vortex shedding ($C_{Pv}(\theta =90^{\circ },t,z)$) (c,f,i) for (a–c) $Re=0.6\times 10^5$, (d–f) $Re=1.5\times 10^5$ and (g–i) $Re=3.5\times 10^5$.

Figure 19

Figure 19. Flow past a circular cylinder: variation of spanwise correlation coefficient $R_{pp}$ with $z/D$ for different $\mbox {{Re}}$ at $\theta =90^{\circ }$ based on (a) $C_{P}$, (b) $\tilde {C}_{P}$ and (c) ${C}_{Pv}$.

Figure 20

Figure 20. The $Re=3.0\times 10^5$ flow past a cylinder: surface distribution of time- and span-averaged (a) coefficient of pressure ($\overline {C}_P$) and (b) skin friction coefficient ($\overline {C}_f$) obtained from meshes M1 ($N_{\theta }=800$) and M2 ($N_{\theta }=1600$).

Figure 21

Table 2. The $Re=3.0\times 10^5$ flow past a circular cylinder: time-averaged coefficient of drag ($\overline {C}_D$), r.m.s. of coefficient of lift ($C_{Lrms}$), non-dimensional vortex shedding frequency ($St$), the circumferential extent of SV ($\theta _{SV}$) and LSB ($\theta _{LSB}$) obtained from two finite element meshes with different spatial resolution along the surface of cylinder.

Figure 22

Figure 21. The $Re=4.0\times 10^5$ flow past a cylinder: time- and span-averaged streamlines for meshes (a) M1($\varDelta _z=0.02D$) and (b) M3 ($\varDelta _z=0.01D$). Also shown are the surface distribution of time- and span-averaged (c) coefficient of pressure ($\overline {C}_P$) and (d) skin friction ($\overline {C}_f$) obtained from meshes M1 and M3.

Figure 23

Figure 22. The $Re=4.0\times 10^5$ flow past a cylinder: variation of time- and span-averaged (a) streamwise component of velocity ($\bar {u}/U_{\infty }$) at $y/D=0$, (b) $\overline {u'u'}$ component of Reynolds stress at $y/D=-0.05$ obtained from meshes M1 ($\varDelta _z=0.02D$) and M3 ($\varDelta _z=0.01D$).

Figure 24

Table 3. Flow past a circular cylinder with $L_z=1D$: time-averaged coefficient of drag ($\overline {C}_D$), r.m.s. of coefficient of lift ($C_{Lrms}$) and non-dimensional vortex shedding frequency ($St$) for $Re=0.4\times 10^5$, $1.0\times 10^5$ and $4.0\times 10^5$ obtained from two finite element meshes with different spatial resolution along the span.

Figure 25

Figure 23. The $Re=4.0\times 10^5$ flow past a cylinder: surface distribution of time- and span-averaged (a) coefficient of pressure ($\overline {C}_P$) and (b) skin friction coefficient ($\overline {C}_f$) obtained with computations on mesh M1, and time step size ${\rm \Delta} t_1=2.5\times 10^{-4}$ and ${\rm \Delta} t_2=5\times 10^{-5}$.

Figure 26

Table 4. The $Re=3900$ flow past a circular cylinder: time-averaged coefficient of drag ($\overline {C}_D$), time-averaged base suction ($-\overline {C}_{Pb}$) and Strouhal number ($St$) obtained from present computations and earlier studies.

Figure 27

Figure 24. The $Re=3900$ flow past a circular cylinder: (a) cross-stream variation of time-averaged streamwise component of velocity ($\bar {u}/U_{\infty }$) and (b) cross-stream variation of $\overline {u'u'}$ component of Reynolds stress at several streamwise locations. Also shown are the variations from earlier studies. The abbreviations are: K, Kravchenko & Moin (2000); P, Parnaudeau et al. (2008); C, Cheng et al. (2017); L, Lehmkuhl et al. (2013).

Figure 28

Figure 25. Flow past a circular cylinder: surface distribution of time- and span-averaged coefficient of pressure ($\overline {C}_P$) for $Re=$ (a) $0.2\times 10^5$, (b) $0.4\times 10^5$ and (c) $4.0\times 10^5$. The abbreviations are: C, Cheng et al. (2017); S & B, Szepessy & Bearman (1992); T, Tani (1964).

Figure 29

Figure 26. Flow past a circular cylinder: surface distribution of time- and span-averaged coefficient of skin friction ($\overline {C}_{f}$) for (a) $Re=0.2\times 10^5$ and (b) $Re=1.0\times 10^5$. The abbreviations are: C, Cheng et al. (2017); A, Achenbach (1968).

Figure 30

Figure 27. Flow past a circular cylinder ($AR=1$) with no-slip condition on the end plates at the lateral boundaries. (a) Close-up view of the finite element mesh in the $x$–$y$ plane. The boundary of the end plate is marked using a blue line. (b) The $Q=1$ isosurface of the instantaneous flow showing the horseshoe vortices in the flow. Only half of the span is shown.

Figure 31

Figure 28. The $Re=4\times 10^5$ flow past a circular cylinder with $L_z=1D$: variation of time-averaged velocity ($u^+$) and $\overline {u'_{r}u'_{\theta }}$ component of Reynolds stress with $y^{+}$ at (a) $\theta =90^{\circ }$, (b) $\theta =116.10^{\circ }$ at $Re=4\times 10^5$. Also shown are the velocity profiles in the viscous sublayer ($u^+=y^{+}$) and log layer ($u^+=\frac {1}{0.41} {\log }_{e}(y^{+}) + 4.4$) for a turbulent boundary layer over a flat plate with zero pressure gradient.

Figure 32

Figure 29. Flow past a circular cylinder with $L_z=1D$: surface distribution of shape factor (H) of the boundary layer for $\mbox {{Re}}=1\times 10^5$ and $\mbox {{Re}}=4\times 10^5$. The LS (black filled circle), turbulent attachment (green filled circle) and turbulent separation (purple filled circle) points are also marked in the figure. C denotes Cheng et al. (2017).