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Topological description of near-wall flows around a surface-mounted square cylinder at high Reynolds numbers

Published online by Cambridge University Press:  29 December 2021

Yong Cao*
Affiliation:
School of Naval Architecture, Ocean and Civil Engineering, Shanghai Jiao Tong University, Shanghai 200240, PR China State Key Laboratory of Ocean Engng, Shanghai Jiao Tong University, Shanghai 200240, PR China Department of Architecture and Building Engineering, Tokyo Institute of Technology, Yokohama 226-8502, Japan
Tetsuro Tamura
Affiliation:
Department of Architecture and Building Engineering, Tokyo Institute of Technology, Yokohama 226-8502, Japan
Dai Zhou*
Affiliation:
School of Naval Architecture, Ocean and Civil Engineering, Shanghai Jiao Tong University, Shanghai 200240, PR China State Key Laboratory of Ocean Engng, Shanghai Jiao Tong University, Shanghai 200240, PR China
Yan Bao
Affiliation:
School of Naval Architecture, Ocean and Civil Engineering, Shanghai Jiao Tong University, Shanghai 200240, PR China
Zhaolong Han
Affiliation:
School of Naval Architecture, Ocean and Civil Engineering, Shanghai Jiao Tong University, Shanghai 200240, PR China
*
†Email addresses for correspondence: yongcao@sjtu.edu.cn, zhoudai@sjtu.edu.cn
†Email addresses for correspondence: yongcao@sjtu.edu.cn, zhoudai@sjtu.edu.cn

Abstract

This study topologically describes near-wall flows around a surface-mounted cylinder at a high Reynolds number ($Re$) of $5\times 10^4$ and in a very thick boundary layer, which were partially measured or technically approximated from the literature. For complete and rational flow construction, we use high-resolution simulations and critical-point theory. The large-scale near-wake vortex is composed of two connected segments rolled up from the sides of the cylinder and from the free end. Another large-scale side vortex clearly roots on two notable foci on the lower side wall. In the junction region, the side vortex moves upwards with a curved trajectory, which induces the formation of nodes on the ground surface. In the free-end region, the side vortex is compressed, which results in a smaller trailing-edge vortex and its downstream movement. Only tip vortices are observed in the far wake. The origin of the tip vortices and their distinction from the near-wake vortex are discussed. Further analyses suggest that $Re$ independence should be treated with high caution when $Re$ increases from 500 to ${O}(10^4)$. The occurrence of upwash flow behind the cylinder strongly depends on the increase in $Re$, the mechanism of which is also provided. The separation–reattachment process in the junction region and the trailing-edge vortices are discovered only at a high $Re$. The former should significantly affect the strength of the side vortex in the junction region and the latter should cause a sharp drop in pressure near the trailing edge.

Information

Type
JFM Papers
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (https://creativecommons.org/licenses/by/4.0/), which permits unrestricted re-use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1. (a) Model of a surface-mounted square cylinder in a turbulent boundary layer when $Re=5\times 10^4$. (b) Grid system in the symmetry plane. (c) Grid system in the x–y plane in the middle of the cylinder. The domain sizes are normalised by D. The cell sizes are also tabbed in different regions relative to the minimum cell size $\varDelta$ immediately near the immersed boundary. Panels (b) and (c) are reproduced from Cao et al. (2019).

Figure 1

Figure 2. One-dimensional energy spectra of the streamwise velocity component in the wake. The measurement station in the present case is located at $(x/D, y/D, x/D) = (1.5, 0, 1.5)$, and those of Trias et al. (2015) are located along the centreline of the wake when $x/D = 1.0$ and 2.5. The vertical dash–dotted line represents the grid cut-off frequency and the blue dashed line represents a slope of $-5/3$.

Figure 2

Figure 3. (a) Time-averaged velocity and turbulence intensity profiles near the inlet as compared with the experiment by Katsumura (Maruyama et al.2013). (b) Power spectrum density at $(x/D, y/D, z/D) =(-7.4, 0, 4)$, where the cell size at this position is approximately $0.03D$. The figures are reproduced from Cao et al. (2019).

Figure 3

Figure 4. (a) Measurement heights in the present study (black lines) and the experiment (red lines). The letters ‘(b)’ and ‘(c)’ with numbers, which appear next to the cylinder, correspond to the subplots in panels (b) and (c), respectively. (b)–(c) Comparison of time-averaged and r.m.s. pressure distributions with the experiment, respectively, which are reproduced from Cao et al. (2019).

Figure 4

Figure 5. Critical-point classification in the chart of p–q, reproduced following Délery (2001).

Figure 5

Figure 6. Skin-friction lines on the ground surface: (a) whole view; (b)–(c) close-up views of Zones A and B. In panel (b), blue indicates positive $\bar {U}$ and red indicates the reverse $\bar {U}$.

Figure 6

Figure 7. Surface flow pattern on the ground surface: (a) the whole view; (b) the close-up view of the central area immediately in front of the cylinder; (c) the close-up view of the central area immediately behind the cylinder and (d) the close-up view of the flow beside the side wall.

Figure 7

Table 1. Locations of the critical points in the surface flow pattern of the ground surface.

Figure 8

Figure 8. Skin-friction lines on the walls of the cylinder when $Re=5\times 10^4$. Panels (a) and (b) show two perspectives. Critical points are $S$, saddle points; $N$, nodal points; and $F$, foci. The dashed lines denote the ($S$) separation and ($A$) attachment lines. (c) Close-up view of the local regions on the side wall, including Zones D, E and F, where blue indicates positive $\bar U$ and red indicates reverse $\bar U$.

Figure 9

Figure 9. Surface flow pattern on the walls of the cylinder in the junction influence region: (a) frontal wall; (b) side wall, with flow from left to right; (c) back wall; (d) close-up view of the local region on the side wall.

Figure 10

Figure 10. Flow visualisation of 3-D separation in the junction region. Panels (a)–(d) are from different perspectives. Here, $S_2$, saddle point on the side wall; $F_1$, focus on the side wall; $SV$, side vortex; $WV$, near-wake vortex; $TEV$, trailing-edge vortex; $SSV$, secondary separation vortex.

Figure 11

Figure 11. Flow topologies projected in the cross-sections at different heights above the secondary horseshoe vortex: (a) $z/D=0.16$; (b) $z/D=0.20$; (c) $z/D=0.28$; (d) $z/D=0.36$. The left-hand column shows the pseudo-streamlines from the numerical results; the right-hand column indicates the flow topology constructed using critical-point concepts, where the bold lines denote the separation lines. The number of critical points is also shown.

Figure 12

Figure 12. Three-dimensional separation surfaces in the junction region, including the near-wake, side, trailing-edge and secondary horseshoe vortices: (a) covered by the outer separation surface; (b) with the removal of the outer separation surfaces.

Figure 13

Figure 13. Surface flow pattern on the walls of the cylinder in the free-end influence region: (a) upper wall; (b) frontal wall; (c) side wall, with flow from left to right; (d) back wall.

Figure 14

Figure 14. Flow visualisation of 3-D separation in the free-end region. Panels (a)–(c) are from different perspectives. Here, $S_7$, saddle point on the side wall; $SV$, side vortex; $WV$, near-wake vortex; $TEV$, trailing-edge vortex; $SSV$, secondary separation vortex. The vortex name followed by ‘-$t$’ denotes the vortex above the top wall (i.e. $TEV$-$t$, side-edge vortex above the top wall; $SSV$-$t$, $SSV$ above the top wall; $SEV$-$t$, side-edge vortex above the top wall.)

Figure 15

Figure 15. Three-dimensional separated flow topology in the free-end influence region. The abbreviations of vortices are referred to the caption of figure 14.

Figure 16

Figure 16. Schematic of mapping the flow above the surface to a closed body: (a) actual flow above the surface, where only one of the node, saddle, half-node and half-saddle points are illustrated; (b) flow region OPXY mapped from the actual flow by flattening OP, and the image system ${O}_i {P}_i {X}_i {Y}_i$ formed by a mirror; (c) closed body with a complexity of zero created by wrapping the region OPXY and ${O}_i {P}_i {X}_i {Y}_i$, where the imaginary upstream and downstream nodes at infinity are added to satisfy the topological principle.

Figure 17

Figure 17. Flow topology in the symmetry plane when $Re=5\times 10^4$. The number of critical points is also shown.

Figure 18

Figure 18. Isosurface of the second invariant of the velocity gradient tensor $QD^2/U_{\infty }^2=0.01$, which is coloured by the streamwise vorticity. Note that the velocity field is filtered by a Gaussian filter with a width of $0.5D$ to clarify the large-scale vortices.

Figure 19

Figure 19. Vorticity source of the tip vortex, where only half of the domain ($y\geq 0$) is shown for clarity. The white 3-D isosurface is $QD^2/U_{\infty }^2=0.01$. The black and red lines are the velocity streamlines, whose source points are located at the centres of two regions of the tip vortex with small and large radii (i.e. $(x/D, y/D, z/D) = (2.5, 0.71, 2.42)$ and (6.0, 1.2, 2.13), indicated by the black and red spheres, respectively). The blue and pink lines are the vortex lines, whose source points are located along the velocity streamlines at a streamwise interval of $1D$. (a) Top view; (b) side view, where the symmetry plane ($y/D=0$) is visualised by the line integral convolution technique and coloured by the lateral vorticity component $\omega _y$; (c) back view.

Figure 20

Figure 20. Quantification of the amount of upwash in the symmetry plane when $z/D\leq 1.0$. The colour indicates the distribution of vertical velocity in the region when $\overline {W}>0$; the region of $\overline {W}<0$ is not considered for the integration.

Figure 21

Figure 21. Relationship between the tip and near-wake vortices. The tip vortex is visualised in the same manner as in figure 19(b). The red line is approximately around the centre of the near-wake vortex. This is the streamline of velocity through the centre of the near-wake vortex in the horizontal plane, specifically at $(x/D, y/D, z/D) = (1.2, 0.53, 2.0)$, as indicated by the black sphere. The green lines are the vorticity lines along the red velocity streamline, which are plotted to illustrate the vorticity source of the near-wake vortex. (a) 3-D perspective, (b) side view and (c) top view.

Figure 22

Figure 22. Distribution of the near-wake vortex core from the 3-D and projected views in the $x$–$z$ and $y$–$z$ planes.

Figure 23

Figure 23. Flow in the $y$–$z$ plane when $x/D=1.0$, where the background greyscale refers to the streamwise velocity.

Figure 24

Figure 24. Compilation of upwash existence in the symmetry plane when $Re \geq 500$ and $H/D=2.7\text {--}18.6$.

Figure 25

Figure 25. Flow topology on the cross-sections of the middle height of the cylinder: (a) $Re=500$, inferred from the flow visualisation of Zhang et al. (2017); (b) $Re=1000$, inferred from the flow visualisation of Zhang et al. (2017); (c) $Re=50\ 000$ in the present study.

Figure 26

Figure 26. Profiles of mean streamwise velocity along the lateral direction: (a) $z/D = 1.0$; (b) $z/D = 1.5$; (c) $z/D = 2.0$. The profiles are shifted downward by 0.5 for the sake of clarity.

Figure 27

Figure 27. (a) Distribution of the ratio between the cube root of cell volume ($\sqrt [3]{V_{cell}}$) and the Kolmogorov length scale ($\eta$) in the region of $x/D = [-1, 6]$, $y/D = [0, 3]$ when $z/D = 1.45$. The cube is indicated, which includes $16\times 16\times 16$ cells in three directions. (b) Histogram of $\sqrt [3]{V_{cell}}/\eta$, where the maximum and mean values are approximately 7.4 and 1.2, respectively.

Figure 28

Figure 28. Temporal convergence of the mean and r.m.s. values of the direction of wall shear stress (denoted by $\theta$) at the cross-section: (a) $z/D=0.40$; (b) $z/D=1.45$; (c) $z/D=2.50$.

Figure 29

Figure 29. Temporal convergence of the mean and r.m.s. values of velocity components in the near wake when $x/D=1.5$: (a) $z/D=0.51$; (b) $z/D=1.50$; (c) $z/D=2.50$.

Figure 30

Figure 30. (a) Cell distribution near the immersed boundary; (b) finite-difference stencil of velocity derivative.

Figure 31

Figure 31. Influence of finite-difference discretisation on the direction of wall shear stress. The cross-section is selected at the middle height of the cylinder.