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Turbulent transport for wall-shear-stress fluctuations

Published online by Cambridge University Press:  24 November 2025

Myoungkyu Lee*
Affiliation:
Department of Mechanical and Aerospace Engineering, University of Houston , Houston, TX, USA
Yongyun Hwang
Affiliation:
Department of Aeronautics, Imperial College London, London SW7 2AZ, UK
*
Corresponding author: Myoungkyu Lee, leemk@uh.edu

Abstract

Statistical structure and the underlying energy budget of wall-shear-stress fluctuations are studied in both Poiseuille and Couette flows with emphasis on its streamwise component. Using a dimensional analysis and direct numerical simulation data, it is shown that the spectra of streamwise wall dissipation for $\lambda \lesssim 1000 \delta _\nu$ are asymptotically invariant with the Reynolds number (${\textit{Re}}$), whereas those for $\lambda \gtrsim \delta$ decay with ${\textit{Re}}$ (here, $\lambda$ is a nominal wall-parallel wavelength, and $\delta _\nu$ and $\delta$ are the viscous inner and outer length scales, respectively). The wall dissipation increases with ${\textit{Re}}$ due to the increasing contribution of the spectra at $1000 \delta _\nu \lesssim \lambda \lesssim \delta$. The subsequent analysis of the energy budget shows that the near-wall motions associated with these wall-dissipation spectra are driven mainly by turbulent transport and are ‘inactive’ in the sense that they contain very little Reynolds shear stress (or turbulence production). As such, turbulent-transport spectra near the wall are also found to share the same ${\textit{Re}}$-scaling behaviour with wall dissipation, and this is observed in the spectra of both the wall-normal and inter-scale turbulent transports. The turbulent transport underpinning the increase of wall dissipation with ${\textit{Re}}$ is characterised by energy fluxes towards the wall, together with inverse energy transfer from small to large length scales along the wall-parallel directions.

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JFM Papers
Creative Commons
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Copyright
© The Author(s), 2025. Published by Cambridge University Press
Figure 0

Figure 1. Two-dimensional spectral densities in polar-log coordinates of $u'^2$ and $\epsilon _{{w}}$, $k_{\textit{ref}} = 1/ (50\,000\delta _v)$: (a) $E_{u'^2}^\#$ at $y^+ = 15$, ${\textit{Re}}_\tau = 5200$, Poiseuille, $\psi = 13$ (b) $E_{\epsilon _{{w}}}^\#$, ${\textit{Re}}_\tau = 5200$, Poiseuille, $\psi = 0.67$ (c) $E_{u'^2}^\#$ at $y^+ = 15$, ${\textit{Re}}_\tau = 500$, Couette, $\psi = 45$ (d) $E_{\epsilon _{{w}}}^\#$, ${\textit{Re}}_\tau = 500$, Couette, $\psi = 4.4$. Here, the contour levels are suitably chosen to reveal the similarities between the spectral densities of $u'^2$ and $\epsilon _{{w}}$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure01/Fig01.ipynb. See § 2 for the mathematical definition of spectral densities in polar-log coordinates.

Figure 1

Figure 2. Inner-scale normalised two-dimensional spectral densities in polar-log coordinates of $\epsilon _{{w}}$ for Poiseuille flows, $k_{\textit{ref}} = 1/ (50\,000\delta _v)$. (a) ${\textit{Re}}_\tau = 550$ (b) ${\textit{Re}}_\tau = 1000$ (c) ${\textit{Re}}_\tau = 2000$ (d) ${\textit{Re}}_\tau = 5200$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure02/Fig02.ipynb.

Figure 2

Figure 3. Outer-scale normalised two-dimensional spectral densities in polar-log coordinates of $\epsilon _{{w}}$ for Poiseuille flows, $k_{\textit{ref}} = 1/ (100\delta )$. (a) ${\textit{Re}}_\tau = 550$ (b) ${\textit{Re}}_\tau = 1000$ (c) ${\textit{Re}}_\tau = 2000$ (d) ${\textit{Re}}_\tau = 5200$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure03/Fig03.ipynb.

Figure 3

Figure 4. Dissipation rate of $\langle u'^2 \rangle ^+$ at walls, $\epsilon _{{w}}$ for Couettte ($\circ$) and Poiseuille ($\square$) flows at various ${\textit{Re}}_\tau$: (a) total and inner-scale-filtered $\epsilon _{{w}}$; (b) inner-scale-filtered $\epsilon _{{w}}$, magnification of (a); (c) outer-scale-filtered $\epsilon _{{w}}$ for Couette flow; (d) outer-scale-filtered $\epsilon _{{w}}$ for Poiseuille flow; (e) difference between $\epsilon _{{w}}$ and the sum of inner-scale-filtered $\epsilon _{{w}}$ and outer-scale-filtered $\epsilon _{{w}}$ (Poiseuille flow for ${\textit{Re}}_\tau \gt 1000$). https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure04/Fig04.ipynb.

Figure 4

Figure 5. Filtered budget terms near the wall of Poiseuille flows. (a,b) Production; (c,d) pressure transport; (e,f) turbulent transport; (g,h) viscous transport; (i,j) dissipation rate. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure05/Fig05.ipynb.

Figure 5

Figure 6. Filtered budget terms near the wall of Couette flows. (a,b) Production; (c,d) pressure transport; (e,f) turbulent transport; (g,h) viscous transport; (i,j) dissipation rate. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure06/Fig06.ipynb.

Figure 6

Figure 7. Inner-scale normalised two-dimensional spectral densities of wall-normal transport and inter-scale transfer of $\langle u'^2\rangle$ in polar-log coordinates, $y^+ = 5$, Poiseuille flows, $k_{\textit{ref}} = 1/ (50\,000\delta _v)$: (a–d) wall-normal transport, $T^\bot$; (e–h) inter-scale transfer $T^\|$. (a) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 550$ (b) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 1000$ (c) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 2000$ (d) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 5200$ (e) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 550$ (f) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 1000$ (g) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 2000$ (h) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 5200$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure07/Fig07.ipynb.

Figure 7

Figure 8. Outer-scale normalised two-dimensional spectral densities of wall-normal transport and inter-scale transfer of $\langle u'^2\rangle$ in polar-log coordinates, $y^+ = 5$, Poiseuille flows, $k_{\textit{ref}} = 1/ (100\delta )$: (a–d) wall-normal transport, $T^\bot$; (e–h) inter-scale transfer $T^\|$. (a) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 550$ (b) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 1000$ (c) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 2000$ (d) $T^\bot_{y^+ = 5}, {\textit{Re}}_\tau = 5200$ (e) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 550$ (f) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 1000$ (g) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 2000$ (h) $T^{\|}_{y^+ = 5}, {\textit{Re}}_\tau = 5200$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure08/Fig08.ipynb.

Figure 8

Figure 9. Turbulent transport near the wall of Poiseuille flow, conditioned with the positive and negative part of the corresponding spectra: (a) wall-normal transport $T^\bot$; (b) inter-scale transfer $T^\|$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure09/Fig09.ipynb.

Figure 9

Figure 10. Turbulent wall-normal transport, $T^+_\bot$, and inter-scale transfer, $T^+_\|$ of $\langle u'^2 \rangle ^+$: (——) $T^+_\bot$, (– – –) $T^+_\|$. (a–b) Inner-scale filtered with $\lambda ^+=1000$; (c–d) outer-scale filtered with $\lambda =\delta$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure10/Fig10.ipynb.

Figure 10

Figure 11. Budget terms, $B^+$, of $\langle u'^2 \rangle^+$ in near-wall regions: P - Poiseuille, C - Couette. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure11/Fig11.ipynb.

Figure 11

Figure 12. Two-dimensional spectral densities of Poiseuille flows in polar-log coordinates of $u'^2$ at $y^+ = 15$, $k_{\textit{ref}} =1/(50\,000\delta _v)$. (a) ${\textit{Re}}_\tau = 550$ (b) ${\textit{Re}}_\tau = 1000$ (c) ${\textit{Re}}_\tau = 2000$ (d) ${\textit{Re}}_\tau = 5200$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure12/Fig12.ipynb.

Figure 12

Figure 13. Two-dimensional spectral densities of Poiseuille flows in polar-log coordinates of $u'^2$ at $y^+ = 15$, $k_{\textit{ref}} =1/(100\delta )$. (a) ${\textit{Re}}_\tau = 550$ (b) ${\textit{Re}}_\tau = 1000$ (c) ${\textit{Re}}_\tau = 2000$ (d) ${\textit{Re}}_\tau = 5200$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure13/Fig13.ipynb.

Figure 13

Figure 14. Streamwise velocity variances: (a,b) (——) $\langle u'^2 \rangle ^+$, (– $\boldsymbol{\cdot}$ –) $\langle u'^2 \rangle ^+_{\lambda ^+\lt 1000}$, (– – –), $\langle u'^2 \rangle ^+_{\lambda ^+\geqslant 1000}$; (c,d) (——), $\langle u'^2 \rangle^+_{\lambda \ge \delta}$. https://multimediafluids.uam.elogim.com/S0022112025108446/JFM-Notebooks/files/figure14/Fig14.ipynb.

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