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Energy dissipation caused by boundary layer instability at vanishing viscosity

Published online by Cambridge University Press:  26 June 2018

Natacha Nguyen van yen
Affiliation:
Institut für Mathematik, Freie Universität Berlin, Arnimallee 6, 14195 Berlin, Germany
Matthias Waidmann
Affiliation:
Institut für Mathematik, Freie Universität Berlin, Arnimallee 6, 14195 Berlin, Germany
Rupert Klein
Affiliation:
Institut für Mathematik, Freie Universität Berlin, Arnimallee 6, 14195 Berlin, Germany
Marie Farge*
Affiliation:
LMD-CNRS, Ecole Normale Supérieure, 24 rue Lhomond, 75231 Paris CEDEX 5, France
Kai Schneider
Affiliation:
Institut de Mathématiques de Marseille, Aix-Marseille Université and CNRS, Marseille, France
*
†Email address for correspondence: marie.farge@ens.fr

Abstract

A qualitative explanation for the scaling of energy dissipation by high-Reynolds-number fluid flows in contact with solid obstacles is proposed in the light of recent mathematical and numerical results. Asymptotic analysis suggests that it is governed by a fast, small-scale Rayleigh–Tollmien–Schlichting instability with an unstable range whose lower and upper bounds scale as $Re^{3/8}$ and $Re^{1/2}$, respectively. By linear superposition, the unstable modes induce a boundary vorticity flux of order $Re^{1}$, a key ingredient in detachment and drag generation according to a theorem of Kato. These predictions are confirmed by numerically solving the Navier–Stokes equations in a two-dimensional periodic channel discretized using compact finite differences in the wall-normal direction, and a spectral scheme in the wall-parallel direction.

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 (http://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
© 2018 The Authors
Figure 0

Figure 1. Imaginary versus real part of the Tietjens function $F(\unicode[STIX]{x1D702})$ for $\unicode[STIX]{x1D702}\in [2,20]$. The sampling points (every $0.1$) are indicated by crosses.

Figure 1

Figure 2. Streamlines of initial velocity field in the subdomain $K=[1/2,1]\times [0,1/2]$.

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Table 1. Definitions and initial values of several integral quantities of interest.

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Table 2. Parameters of numerical experiments. All figures in this table are given up to three significant digits.

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Figure 3. Schematics of discretization grids used by the Navier–Stokes solver for $t\leqslant 54$ (a) and $t>54$ (b). The thickness of the various regions is computed from the Reynolds number as summarized in table 2.

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Figure 4. Comparison between Navier–Stokes at $Re=123\,075$ (black) and Euler/Prandtl (blue). (a,b) Contour lines of vorticity field at $t=30$ (a) and $t=50$ (b), for $\unicode[STIX]{x1D714}=0.1,0.2,\ldots ,1$. (c,d) Contour lines of corresponding boundary layer vorticity fields in Prandtl variables, for $\unicode[STIX]{x1D714}=-|\unicode[STIX]{x1D714}|_{max}/6,-2|\unicode[STIX]{x1D714}|_{max}/6,\ldots ,-5|\unicode[STIX]{x1D714}|_{max}/6$, where $|\unicode[STIX]{x1D714}|_{max}=3.75\times 10^{-4}$ and $|\unicode[STIX]{x1D714}|_{max}=8.70\times 10^{-3}$, respectively.

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Figure 5. Contour lines of vorticity field in Prandtl variables at $t=54$ (a) and $t=55.3$ (b), for $\unicode[STIX]{x1D714}=5|\unicode[STIX]{x1D714}|_{max}/6,\ldots ,|\unicode[STIX]{x1D714}|_{max}/6,0,-|\unicode[STIX]{x1D714}|_{max}/6,-2|\unicode[STIX]{x1D714}|_{max}/6,\ldots ,-5|\unicode[STIX]{x1D714}|_{max}/6$, where $|\unicode[STIX]{x1D714}|_{max}=1.25\times 10^{-2}$ and $|\unicode[STIX]{x1D714}|_{max}=1.30\times 10^{-2}$, respectively. Black contour lines correspond to Navier–Stokes at $Re=123\,075$, while blue lines correspond to Euler/Prandtl. The $\unicode[STIX]{x1D714}=0$ contour line is shown in bold.

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Figure 6. Comparison between Navier–Stokes (black), Prandtl–Euler (blue) and interactive boundary layer (red) models at $t=50$ (a) and $t=54$ (b). Contour lines of vorticity (a,b) and vorticity along the boundary (c,d). The $\unicode[STIX]{x1D714}=0$ contour line is shown in bold.

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Figure 7. Vorticity along the boundary for Navier–Stokes (solid line) for varying Reynolds number (from $Re=7692$ to $123\,075$) and Prandtl (dashed line).

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Figure 8. Fourier spectra of boundary vorticity for Navier–Stokes (solid line) at different Reynolds numbers (from $Re=7692$ to $123\,075$) and Prandtl (dashed line). The spectra have been smoothed to eliminate fast oscillations due to the odd symmetry of the function (see text).

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Figure 9. Stability boundary subject to the frozen flow approximation, shown as a function of $x$ at $t=54$ and for $Re=123\,075$. The upper and lower marginal wavenumbers estimated from our asymptotic analysis (2.51) and (2.54) are shown in dashed lines.

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Figure 10. Contour lines of vorticity field in Prandtl variables for Navier–Stokes at $t=56$ (a) and $t=56.9$ (b). The $\unicode[STIX]{x1D714}=0$ contour line is shown in bold.

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Figure 11. Vorticity along the boundary for various Reynolds numbers (from $Re=7692$ to $123\,075$) in Prandtl variables at $t=56$ (a) and $t=56.9$ (b).

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Figure 12. Reynolds-number scalings of maximum vorticity (a) and enstrophy (b) for Prandtl and Navier–Stokes before detachment ($t=53$), and for Navier–Stokes after detachment ($t=56.9$).

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Figure 13. Contour lines of vorticity field at $t=80$ for Navier–Stokes at $Re=15\,384$ and Euler/Prandtl solutions.

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Figure 14. Comparison between Navier–Stokes solutions at the same Reynolds number ($Re=123\,075$) with two numerical resolutions, in order to check for convergence: (a) $t=56$, (b) $t=56.9$.

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Table 3. Location $(x_{d},y_{d})$ and value $(\unicode[STIX]{x1D714}_{d})$ of maximum vorticity for various times and Reynolds numbers, compared to the data in table III of Kramer et al. (2007), for the dipole–wall test case.

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Figure 15. Wall shear stress at different instants for the impulsively started cylinder test case.

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Figure 16. Unstable region for the Blasius boundary layer.

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Figure 17. Vorticity fields for the Navier–Stokes solution (left) and the Euler solution (right) in the bulk flow at $t=30,50$ and $55.1$. The corresponding vorticity fields in the boundary layer for the Navier–Stokes (left) and the Prandtl solutions (right) are given directly below. The corresponding movie can be downloaded from https://doi.org/10.1017/jfm.2018.396.

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Figure 18. Continuation of figure 17 at time instants $t=57$ and $100$. The Prandtl solution is singular and thus not shown. The corresponding movie can be downloaded from https://doi.org/10.1017/jfm.2018.396.

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Figure 19. Vorticity along the boundary at $t=30,~50,~55.1$ and $57$.

Nguyen van yen et al. supplementary movie

Time evolution, from $t=0$ to $90$, of the vorticity field in the bulk flow for the Euler solution (left) and the Navier--Stokes solution (right). The Prandtl solution becomes singular at $t^{\star}=55.6$ and is thereafter not shown. The corresponding vorticity field in the boundary layer for the Prandtl solution (left) and the Navier--Stokes solution (right) are given directly below.

Download Nguyen van yen et al. supplementary movie(Video)
Video 5 MB