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Nonlinear optimal perturbation of turbulent channel flow as a precursor of extreme events

Published online by Cambridge University Press:  29 August 2023

N. Ciola*
Affiliation:
DMMM, Politecnico di Bari, Via Re David 200, 70125 Bari, Italy DynFluid, Arts et Métiers Paris/CNAM, 151 Bd de l'Hôpital, 75013 Paris, France
P. De Palma
Affiliation:
DMMM, Politecnico di Bari, Via Re David 200, 70125 Bari, Italy
J.-C. Robinet
Affiliation:
DynFluid, Arts et Métiers Paris/CNAM, 151 Bd de l'Hôpital, 75013 Paris, France
S. Cherubini
Affiliation:
DMMM, Politecnico di Bari, Via Re David 200, 70125 Bari, Italy
*
†Email address for correspondence: n.ciola@phd.poliba.it

Abstract

This work aims at studying the mechanisms behind the occurrence of extreme dissipation events in a channel flow, identifying nonlinear optimal perturbations as potential precursors of these events. Nonlinear optimal perturbations with respect to a generic turbulent instantaneous snapshot are computed for the first time using a direct-adjoint algorithm in the channel flow at $Re_{\tau }\approx 180$. The resulting initial perturbation displays the upstream tilting characteristic of Orr's mechanism and is positioned along the interfaces between two opposite-sign velocity streaks of the pre-existing turbulent field. Such a perturbation induces a sudden breakdown of the pre-existing structures and a heavier tail in the dissipation probability density function distribution. Different mechanisms are at play during this process: the high shear present at the interface between coherent low- and high-momentum regions is exploited to break down the larger structures and drive energy to small scales. This energy cascade is fed by an enhanced lift-up effect that produces intense streaks near the wall. It is found that the optimal perturbation grows exponentially during the first phase of its evolution reflecting the existence of a secondary modal instability of the streaks. To corroborate the results, the conditional spatiotemporal proper orthogonal decomposition (POD) analysis of Hack & Schimdt (J. Fluid Mech., vol. 907, 2021, A9) is performed both in the perturbed and in the unperturbed flow, showing a clear agreement between the two cases and with the reference study. Thus, the optimal perturbation at initial time can be considered as a precursor of extreme events.

Information

Type
JFM Papers
Copyright
© The Author(s), 2023. Published by Cambridge University Press
Figure 0

Figure 1. Convergence plot of the nonlinear turbulent optimisation. The solid line indicates the objective function (2.2) (right axis); the dashed line indicates $tol=(\mathcal {J}^n-\mathcal {J}^{n-1})/\mathcal {J}^{n-1}$; and the dotted line indicates the convergence ratio (3.2a–c) (left axis).

Figure 1

Figure 2. Optimal streamwise velocity perturbation isocontours ($\lvert \tilde {\boldsymbol{u}} \rvert =0.02, \lvert \tilde {\boldsymbol{u}} \rvert _{max}\approx 0.21$), red/blue for positive/negative.

Figure 2

Figure 3. Contours of the pre-multiplied spectrum of the streamwise component of the perturbation $\tilde {\boldsymbol{u}}(t_0=300)$ at $y^+=10$ (log scale). The starred point is $k_x^+=5.56\times 10^{-3}$, $k_z^+=2.22\times 10^{-2}$.

Figure 3

Figure 4. Top view of the optimal streamwise velocity perturbation isocontours (as in figure 2). The green lines highlight the romboidal pattern.

Figure 4

Figure 5. Distribution of the optimal streamwise perturbation (shaded contours) superposed to the filtered streaks of the unperturbed flow at $t_0$ (white lines, solid for positive and dashed for negative) in the $y^+=10$ plane. The top-left panel is the whole domain, the others are details of the same figure. The streaks are obtained filtering the unperturbed flow and retaining modes between $0.02< k_x^+<0.05$ and $0.03< k_z^+<0.1$.

Figure 5

Figure 6. Contours of the dissipation at $t=t_0+T=302$ on the $y^+=10$ plane. Top left: unperturbed flow. Top right: optimally perturbed flow. Bottom: two examples of locally perturbed flow.

Figure 6

Figure 7. Contours of the streamwise perturbation $\tilde {u}(\boldsymbol {x},t) = u_p(\boldsymbol {x},t) - u_u(\boldsymbol {x},t)$ for an artificially localised optimal perturbation. Top: contours of the streamwise perturbation superposed to the filtered streaks of the unperturbed flow at $t_0$ (white lines, solid for positive and dashed for negative) in the $y^+=10$ plane; the right frame shows a close-up of the left frame. Bottom: contours of the streamwise perturbation on the same plane at $t=302,305$.

Figure 7

Figure 8. Time history of the volume-averaged TKE (a,d), dissipation (b,e) and friction Reynolds number (c,f). Four flows are compared: the optimally perturbed flow (green line); the unperturbed flow (dashed black line); the flow perturbed by a non-optimal perturbation (blue line); the flow perturbed by a linear optimal perturbation with same initial energy (red line). The top line refers to the initial snapshot $t_0=300$, whereas the bottom line refers to $t_0=360$.

Figure 8

Figure 9. Time evolution of the turbulent split production on different horizontal planes. (a) Lift-up-like production $\left \langle \mathcal {P}_{lu} \right \rangle _z$. (b) Orr-like production $\left \langle \mathcal {P}_{Orr} \right \rangle _x$. Solid lines are the optimally perturbed flow, dashed lines the unperturbed flow.

Figure 9

Figure 10. Time evolution of the flow averaged along the streamwise direction: isocontours of the streamwise velocity component and arrows for the transverse components. From top to bottom $t=[t_0, t_0+1, t_0+2, t_0+5]$. From left to right: perturbed flow, unperturbed flow, perturbation. For the first two columns the streamwise component refers to the turbulent fluctuation, i.e. the instantaneous velocity minus the turbulent mean profile.

Figure 10

Figure 11. Spacetime plots of the turbulent split production. Solid black lines are the baseflow production contours (solid for positive values, dashed for negative) while shaded contours are the increment due to the perturbation ($\mathcal {P}_{lu/Orr}^p-\mathcal {P}_{lu/Orr}^u$): (a,c) $y^+=10$ plane; (b,d) $y^+=30$ plane; (a,b) lift-up-like production $\mathcal {P}_{lu}$; (c,d) Orr-like production $\mathcal {P}_{Orr}$.

Figure 11

Figure 12. (a,b) Time evolution of the perturbation energy $1/2\left \langle \tilde {\boldsymbol{u}}, \tilde {\boldsymbol{u}} \right \rangle$ for different realisations of the perturbed flow. The dashed blue line is the evolution for a flow perturbed with a random non-optimal perturbation. (c,d) Time evolution of the individual perturbation energy budgets $1/2\left \langle \tilde {u}^2 \right \rangle$, $1/2\left \langle \tilde {v}^2 \right \rangle$ and $1/2\left \langle \tilde {w}^2 \right \rangle$ (colours as in top panels). The right panels are the dashed black rectangles magnified. The growth rate correspondent to the dashed black line in the top right panel is $\approx 3.69 U_b/h$ for the energy, i.e. ${\approx }1.84 U_b/h$ for the perturbation amplitude.

Figure 12

Figure 13. Probability density function of the local dissipation normalised with the respective standard deviation for the optimally perturbed flow (solid green line) and the unperturbed flow (dashed black): (a) $y^+=10$ plane; (b) $y^+=30$ plane. The solid red line is for the flow perturbed with a linear optimal perturbation.

Figure 13

Figure 14. (a) Turbulent attractor projected on the TKE–dissipation plane: reference DNS (solid grey line), optimally perturbed flow (solid blue) and locally perturbed flows (solid black). (b) Dissipation p.d.f. sampled on the perturbed zone in the locally perturbed flows (solid green line) and on the corresponding points in the unperturbed flow (dashed black) on the $y^+=10$ plane.

Figure 14

Figure 15. Distribution of the 30 leading eigenvalues of the POD. (a) Unperturbed flow. (b) Optimally perturbed flow.

Figure 15

Figure 16. Leading POD modes of the extreme events: streamwise fluctuation contours. From top to bottom: transverse view of the leading antisymmetric mode, transverse view of the leading symmetric mode, longitudinal view of the leading symmetric mode (the longitudinal view of the antisymmetric mode is not relevant). (a,c,e) Unperturbed flow. (b,d,f) Optimally perturbed flow.

Figure 16

Figure 17. Validation of the turbulent production splitting. Perturbation evolved around the turbulent mean flow. The streaks on the left show only non-zero lift-up-like production (solid lines) while the Orr-like perturbation on the right shows only non-zero Orr-like production (dashed lines).