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Transient states in plane Couette flow

Published online by Cambridge University Press:  30 September 2020

D. De Souza
Affiliation:
IMSIA UMR 9219, ENSTA-Paris, CNRS, CEA, EDF, Institut Polytechnique de Paris, 828 Boulevard des Maréchaux, 91762Palaiseau CEDEX, France
T. Bergier
Affiliation:
IMSIA UMR 9219, ENSTA-Paris, CNRS, CEA, EDF, Institut Polytechnique de Paris, 828 Boulevard des Maréchaux, 91762Palaiseau CEDEX, France
R. Monchaux*
Affiliation:
IMSIA UMR 9219, ENSTA-Paris, CNRS, CEA, EDF, Institut Polytechnique de Paris, 828 Boulevard des Maréchaux, 91762Palaiseau CEDEX, France
*
†Email address for correspondence: monchaux@ensta.fr

Abstract

We present the rich and complex relaxation dynamics of turbulent plane Couette flow when the Reynolds number is lowered. In particular, we reveal the existence of well-defined transient states around which the dynamics of turbulent retreat is organized. We characterize these states in physical space and we propose a projection of these states in phase space to understand their nature. The results presented have been obtained in an experiment in which we perform annealing and quenching, i.e. gentle or sudden decreases in Reynolds number. The nature of asymptotic states is also studied and shown to depend on the final Reynolds number, but not at all on the rate of change of the Reynolds number.

Information

Type
JFM Papers
Copyright
© The Author(s), 2020. Published by Cambridge University Press
Figure 0

Figure 1.$(a)$ General sketch of the experimental device of plane Couette flow. A typical velocity field in the streamwise direction obtained by particle image velocimetry (PIV) is superimposed on it. The PIV field is given to scale, which shows that the PIV window fills the whole volume of the experiment. $(b)$ Sketch of the transition diagram as a function of $Re$ and of the aspect ratio. Figure inspired by Philip & Manneville (2011) where the directed percolation regime has been added in the vicinity of $Re_g$ for very high aspect ratio systems. The order parameter in this figure is the turbulent fraction $F_t$ defined in almost 2-D flows as the proportion of the flow area parallel to the walls that is turbulent.

Figure 1

Figure 2.Succession of snapshots of the streamwise velocity $U_x$ along a typical annealing from $Re_i=430$ to $Re_f=300$ at a rate $\dot {Re}=0.3\ \textrm {s}^{-1}$. Time is given in units of $h/U_i$. Colour bars are identical for all velocity contour plots in this article. Ticks are equispaced by 25 units of $h$. $(a) \ t = 0, \ (b) \ t = 6500\,h/U, \ (c) \ t = 2600\,h/U, \ (d) \ t = 9100\,h/U,$$(e) \ t = 3900\,h/U, \ (\,f) \ t = 10\,400\,h/U, \ (g) \ t = 5200\,h/U \ {\rm and}$$(h) \ t = 11\,700\,h/U$.

Figure 2

Figure 3.Turbulent fraction versus time for all $Re_f$ for four different $\dot {Re}$ values. Final Reynolds numbers $Re_f$ are indicated in $(d)$. Traces with the same colour correspond to various experiments performed with the same parameters. In panel $(d)$, the bars labelled with values of $Re_f$ indicate the span of $F_t$ values reached asymptotically between different realizations with the same parameters. See figure 6 for a more quantitative picture. $(a) \ {\rm Quench}, \ (b) \ \dot{R}e = 5, \ (c)\ \dot{R}e = 1 \ {\rm and} \ (d) \ \dot{R}e = 0.3.$

Figure 3

Figure 4.Turbulent fraction versus time for all $\dot {Re}$ for four different $Re_f$ values. Traces with the same colour correspond to various experiments performed with the same parameters. Vertical dash-dotted lines indicate $t_f$, the time at which the final Reynolds number $Re_f$ is reached. For quenches, this line is sometimes hidden by the ordinate axis. $(a) \ \textit{Re}_{f} = 300, \ (b) \ \textit{Re}_{f} = 320, \ (c) \ \textit{Re}_{f} = 340 \ {\rm and} \ (d) \ \textit{Re}_{f} = 360.$

Figure 4

Figure 5.Turbulent fraction versus rescaled time $t\dot {Re}$ for all $\dot {Re}$ for four different $Re_f$ values. Traces with the same colour correspond to various experiments performed with the same parameters. Vertical dash-dotted lines indicate $t_f$, the time at which the final Reynolds number $Re_f$ is reached. Note that with this scaling they occur at the same $t\dot {Re}$ value for all experiments performed at the same $Re_f$, regardless of $\dot {Re}$ value. Quenches are not presented here because, due to our experimental protocol, the time rescaling used here is not relevant for quenches. $(a) \ \textit{Re}_{f} = 300, \ (b) \ \textit{Re}_{f} = 320, \ (c) \ \textit{Re}_{f} = 340 \ {\rm and} \ (d) \ \textit{Re}_{f} = 360.$

Figure 5

Figure 6.$(a)$ Asymptotic turbulent fraction $\overline {F_t}$ as a function of $Re_f$ for various $\dot {Re}$. Error bars represent the dispersion between experiments performed with the same control parameter values. Data from Duguet et al. (2010) are also presented. $(b)$ Time average of the moving standard deviation calculated over time intervals of 15 s. This quantity measures the level of fluctuations around the smoothed dynamics.

Figure 6

Figure 7.(a) Some particular turbulent fraction dynamics picked up to illustrate the robustness of the plateaus. Traces are coloured according to $\dot {Re}$ as in figure 4, continuous lines are for $Re_f=300$, dash-dotted lines for $Re_f=320$. (b,c) Typical velocity fields associated with turbulent fraction plateau at $F_t\simeq 0.5$ (b) and $F_t\simeq 0.1$ (c). They respectively correspond to experiments performed at $\dot {Re}=0.3$ and $\dot {Re}=1$ for a common $Re_f=300$.

Figure 7

Figure 8.Turbulent fraction versus Reynolds number. The continuous blue line is the ensemble average of data from figure 5 obtained for $Re_f=300$ and $\dot {Re}=0.1$, in this case $Re$ is the current Reynolds number. Black symbols with error bar are the ensemble average and standard deviation of data displayed in figure 6, in this case $Re$ is the final Reynolds number. See text for details.

Figure 8

Figure 9.Typical power spectral density of $u_z$ averaged azimuthally for a flow containing bands (as in figure 7b) or a spot (as in figure 7c). They respectively correspond to experiments performed at $\dot {Re}=0.3$ and $\dot {Re}=1$ for a common $Re_f=300$. Turbulent streaks produce a rise in energy in a band of $\lambda /h\in [10^0\text {--}10^1]$ while large-scale flows produce energy for $\lambda /h\in [3\times 10^1\text {--}2\times 10^2]$.

Figure 9

Figure 10.Phase portrait presenting three representative trajectories in the plane ($F_t(t),A_{LSF}(t)$). Snapshots along these three paths are also shown to illustrate the differences between them. From top to bottom, turbulent fraction is 1, 0.9, 0.7, 0.5, 03 and 0.1. Panel frames are coloured according to the followed path.