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Flow past a transversely rotating sphere at Reynolds numbers above the laminar regime

Published online by Cambridge University Press:  30 October 2014

Eric K. W. Poon*
Affiliation:
Department of Mechanical Engineering, University of Melbourne, Parkville, Victoria 3010, Australia
Andrew S. H. Ooi
Affiliation:
Department of Mechanical Engineering, University of Melbourne, Parkville, Victoria 3010, Australia
Matteo Giacobello
Affiliation:
Air Vehicles Division, Defence Science and Technology Organisation, 506 Lorimer Street, Fishermans Bend, Victoria 3207, Australia
Gianluca Iaccarino
Affiliation:
Department of Mechanical Engineering, Stanford University, 488 Escondido Mall, Bldg 02-500, Rm 500A, Stanford, CA 94305-3035, USA
Daniel Chung
Affiliation:
Department of Mechanical Engineering, University of Melbourne, Parkville, Victoria 3010, Australia
*
†Email address for correspondence: epoon@unimelb.edu.au
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Abstract

The flow past a transversely rotating sphere at Reynolds numbers of $\mathit{Re}=500{-}1000$ is directly simulated using an unstructured finite volume collocated code. The effect of rotation rate on the flow is studied by increasing the dimensionless rotation rate, ${\it\Omega}^{\ast }$ , from 0 to 1.20, where ${\it\Omega}^{\ast }$ is the maximum sphere surface velocity normalised by the free stream velocity. This study investigates the marked unsteadiness of the flow structures at $\mathit{Re}=500{-}1000$ . Comparison with previous numerical data (Giacobello et al., J. Fluid Mech., vol. 621, 2009, pp. 103–130; Kim, J. Mech. Sci. Technol., vol. 23, 2009, pp. 578–589) reveals a new flow regime, namely a ‘shear layer–stable foci’ regime, besides the widely reported ‘vortex shedding’ and ‘shear layer instability’ regimes. The ‘shear layer–stable foci’ regime is observed at $\mathit{Re}=500$ and ${\it\Omega}^{\ast }=1.00$ ; $\mathit{Re}=640{-}1000$ and ${\it\Omega}^{\ast }\geqslant 0.80$ . In this flow regime, the shear layer on the advancing side of the sphere (where the sphere surface velocity vector opposes the free stream velocity) shortens significantly while fluid from the retreating side (opposite to the advancing side) is drawn towards the mid-plane normal to the peripheral velocity. This results in the formation of a stable focus near the onset of the shear layer instability. This stable focus becomes more pronounced with increasing $\mathit{Re}$ and ${\it\Omega}^{\ast }$ . It increases the oscillation magnitude and decreases the oscillation frequency of the hydrodynamic forces.

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© 2014 Cambridge University Press 
Figure 0

Figure 1.The problem geometry and coordinate system used in CDP. The sphere is constrained to rotate in the transverse direction.

Figure 1

Figure 2.The unstructured-grid computational domain. (a) Isometric view, (b) $(x,z)$-plane view and (c) $(x,y)$-plane view downstream of the sphere showing the diamond centre section.

Figure 2

Table 1.The sensitivity of the spatial resolution and comparison of the important flow parameters for $\mathit{Re}=500$. The time-averaged drag coefficient, $C_{D}$, lift coefficient, $C_{L}$, Strouhal number, $St$, non-dimensional wake length, $w^{\ast }$ (distance between the sphere centre and the tail of the recirculation bubbles), and separation angle, ${\it\theta}_{s}$, are listed. E stands for experimental data, S for numerical data and C for correlations.

Figure 3

Figure 3.The boundary layer velocity profile for the flow past a stationary sphere at $\mathit{Re}=500$ and 1000. (a) Linear–linear scale and (b) linear–log scale to emphasise the adequate spatial resolution in the viscous sublayer.

Figure 4

Table 2.The sensitivity of the spatial resolution and comparison of the important flow parameters for $\mathit{Re}=1000$. The time-averaged drag coefficient, $C_{D}$, lift coefficient, $C_{L}$, Strouhal number, $St$, non-dimensional wake length, $w^{\ast }$ (distance between the sphere centre and the tail of the recirculation bubbles), and separation angle, ${\it\theta}_{s}$, are listed. E stands for experimental data, S for numerical data and C for correlations.

Figure 5

Figure 4.Centreline velocity for $\mathit{Re}=1000$. (a) Time-averaged centreline velocity and (b) RMS centreline velocity.

Figure 6

Figure 5.The velocity deficit along the $x$ direction at 5 diameters and 10 diameters downstream for $\mathit{Re}=1000$. (a) Time-averaged velocity deficit and (b) RMS streamwise velocity. $\text{}^{(1)}$ Present study and $\text{}^{(2)}$ Tomboulides & Orszag (2000).

Figure 7

Figure 6.Maximum instantaneous viscous wall unit $({\rm\Delta}{r^{+}}_{max})$ of all wall-adjacent cells for (a) $\mathit{Re}=500$ and (b) $\mathit{Re}=1000$.

Figure 8

Figure 7.The ratio of the grid spacing in the $z$ direction, ${\rm\Delta}z$, to the Kolmogorov length scale, ${\it\eta}$, at various locations downstream of the sphere for (a) $\mathit{Re}=1000$, ${\it\Omega}^{\ast }=0.00$ and (b) $\mathit{Re}=1000$, ${\it\Omega}^{\ast }=1.20$.

Figure 9

Figure 8.Different flow regimes for a transversely rotating sphere for low to moderate Reynolds numbers: ⬥, steady flow; +, oscillation vortex threads; ▴, vortex shedding; ○, shear layer instability; ▿, turbulent flow with laminar boundary layer; ▫, shear layer–stable foci. Symbols in grey represent data in the open literature. Symbols in red indicate the newly discovered regime. A representation of the isosurface of the instantaneous vortical structures for selected regime is also presented. Data for $\mathit{Re}\leqslant 300$ are obtained from Kim (2009), Giacobello et al. (2009) and Poon et al. (2010, 2013).

Figure 10

Figure 9.The vortex shedding regime ($\mathit{Re}=500$ and ${\it\Omega}^{\ast }=0.20$): temporal evolution of vortical structures (isosurfaces of ${\it\lambda}_{2}=-0.0008$) over a shedding period. Snapshot of out-of-plane vorticities, ${\it\omega}_{i}$, where the subscript $i=x$, $y$ and $z$, in the $(y,z)$-plane, the $(x,z)$-plane and a cross-stream plane at $z^{\ast }=5$; the projected streamline patterns in the $(y,z)$-plane are also shown. The projected streamlines are coloured by the out-of-plane velocity, $u_{x}$.

Figure 11

Figure 10.(a) The effect of ‘vortex shedding’ on the near-wake streamline pattern and RMS pressure; (b) normalised cross-correlations, $R$, versus time delay, ${\it\tau}$, (see (4.2)) at $z^{\ast }=1.0$ (indicated by the red dashed line in a) for four azimuthal locations (see inset).

Figure 12

Figure 11.Shear layer instability ($\mathit{Re}=500$ and ${\it\Omega}^{\ast }=0.80$): temporal evolution of vortical structures (isosurfaces of ${\it\lambda}_{2}=-0.0008$) over a shedding period. Snapshot of out-of-plane vorticities, ${\it\omega}_{i}$, where the subscript $i=x$, $y$ and $z$, in the $(y,z)$-plane, $(x,z)$-plane and a cross-stream plane at $z^{\ast }=5$; projected streamline patterns in the $(y,z)$-plane are also shown. The projected streamlines are coloured by the out-of-plane velocity, $u_{x}$.

Figure 13

Figure 12.(a) The effect of ‘shear layer instability’ on the near-wake streamline pattern and RMS pressure; (b) normalised cross-correlations, $R$, versus time delay, ${\it\tau}$, (see (4.2)) at $z^{\ast }=1.0$ (indicated by the red dashed line in a) for four azimuthal locations (see inset).

Figure 14

Figure 13.‘Shear layer–stable foci’ regime ($\mathit{Re}=500$ and ${\it\Omega}^{\ast }=1.00$): temporal evolution of vortical structures (isosurfaces of ${\it\lambda}_{2}=-0.0008$) over a shedding period. Snapshot of out-of-plane vorticities, ${\it\omega}_{i}$, where the subscript $i=x$, $y$ and $z$, in the $(y,z)$-plane, $(x,z)$-plane and a cross-stream plane at $z^{\ast }=5$; projected streamline patterns in the $(y,z)$-plane are also shown. The projected streamlines are coloured by the out-of-plane velocity, $u_{x}$.

Figure 15

Figure 14.(a) The effect of ‘shear layer–stable foci’ on the near-wake streamline pattern and RMS pressure; (b) normalised cross-correlations, $R$, versus time delay, ${\it\tau}$, (see (4.2)) at $z^{\ast }=1.0$ (indicated by the red dashed line in a) for four azimuthal locations (see inset).

Figure 16

Figure 15.Effect of Reynolds number on the ‘shear layer–stable foci’ ($\mathit{Re}=1000$ and ${\it\Omega}^{\ast }=1.20$) vortical structures (isosurfaces of ${\it\lambda}_{2}=-0.0008$) over a shedding period. Snapshot of out-of-plane vorticities, ${\it\omega}_{i}$, where the subscript $i=x$, $y$ and $z$, in the $(y,z)$-plane, $(x,z)$-plane and a cross-stream plane at $z^{\ast }=5$; projected streamline patterns in the $(y,z)$-plane are also shown. The projected streamlines are coloured by the out-of-plane velocity, $u_{x}$.

Figure 17

Figure 16.(a) Phase diagram $(C_{Ly},C_{Lx})$ and (b) phase diagram $(C_{L},C_{D})$ for a transversely rotating sphere at $\mathit{Re}=500$.

Figure 18

Figure 17.(a) Phase diagram $(C_{Ly},C_{Lx})$ and (b) phase diagram $(C_{L},C_{D})$ for a transversely rotating sphere at $\mathit{Re}=1000$.

Figure 19

Figure 18.Time-averaged force coefficients for the flow past a stationary and transversely rotating sphere at $\mathit{Re}=500{-}1000$: (a) $\overline{C_{Lx}}$ against ${\it\Omega}^{\ast }$; (b) $\overline{C_{Ly}}$ against ${\it\Omega}^{\ast }$; (c) $\overline{C_{D}}$ against ${\it\Omega}^{\ast }$. The effect of integration time on the time-averaged force coefficients is shown in the insets for a sample parameter $(\mathit{Re}=500\text{ and }{\it\Omega}^{\ast }=0.60)$. Time-averaged force coefficients are displayed at half integration time and full integration time.

Figure 20

Figure 19.Time-averaged resultant force coefficients against Reynolds number for the flow past a stationary and transversely rotating sphere: (a) $\overline{C_{D}}$ and (b) $\overline{C_{Ly}}$. The grey box highlights the change in behaviour in $\overline{C_{Ly}}$ with $\mathit{Re}$.

Figure 21

Figure 20.RMS force coefficients for the flow past a stationary and transversely rotating sphere at $\mathit{Re}=500{-}1000$: (a) ${C_{Lx}}^{\prime }$ against ${\it\Omega}^{\ast }$; (b) ${C_{Ly}}^{\prime }$ against ${\it\Omega}^{\ast }$; (c) ${C_{D}}^{\prime }$ against ${\it\Omega}^{\ast }$.

Figure 22

Figure 21.Strouhal number, $St$, versus dimensionless rotation rate, ${\it\Omega}^{\ast }$, for a transversely rotating sphere.

Figure 23

Figure 22.Instantaneous vortical structures for a transversely rotating sphere at $\mathit{Re}=500$ and 1000. The isosurfaces are identified using the ${\it\lambda}_{2}$ vortex identification and coloured by the streamwise vorticity, ${\it\omega}_{z}$.