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Zonal jets at the laboratory scale: hysteresis and Rossby waves resonance

Published online by Cambridge University Press:  11 January 2021

Daphné Lemasquerier*
Affiliation:
Aix Marseille Univ, CNRS, Centrale Marseille, IRPHE, Marseille, 13013, France
B. Favier
Affiliation:
Aix Marseille Univ, CNRS, Centrale Marseille, IRPHE, Marseille, 13013, France
M. Le Bars
Affiliation:
Aix Marseille Univ, CNRS, Centrale Marseille, IRPHE, Marseille, 13013, France
*
†Email address for correspondence: lemasquerier.pro@protonmail.com

Abstract

The dynamics, structure and stability of zonal jets in planetary flows are still poorly understood, especially in terms of coupling with the small-scale turbulent flow. Here, we use an experimental approach to address the questions of zonal jets formation and long-term evolution. A strong and uniform topographic $\beta$-effect is obtained inside a water-filled rotating tank thanks to the paraboloidal fluid free upper surface combined with a specifically designed bottom plate. A small-scale turbulent forcing is performed by circulating water through the base of the tank. Time-resolving particle image velocimetry measurements reveal the self-organization of the flow into multiple zonal jets with a strong instantaneous signature. We identify a subcritical bifurcation between two regimes of jets depending on the forcing intensity. In the first regime, the jets are steady, weak in amplitude, and directly forced by the local Reynolds stresses due to our forcing. In the second one, we observe highly energetic and dynamic jets of width larger than the forcing scale. An analytical modelling based on the quasi-geostrophic approximation reveals that this subcritical bifurcation results from the resonance between the directly forced Rossby waves and the background zonal flow.

Information

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1. Schematic of the experimental set-up. A cylindrical tank of 1 m in diameter and 1.6 m in height, filled with 600 l of water, is fixed on a table rotating at 75 RPM. The fluid free surface takes a paraboloidal shape due to the centrifugally induced pressure. The bottom plate is designed to achieve a uniform topographic $\beta$-effect. A small-scale turbulent forcing is performed by circulating water through 128 holes at the base of the tank. The forcing pattern is sketched on the right: each ring C1–C6 is controlled by an independent pump. Time-resolving PIV measurements are performed on a horizontal plane using a side green laser and a top-view camera.

Figure 1

Figure 2. (a) Experimental set-up at rest. The tank is mounted on a rotating table operating using an air cushion. It is filled with $\sim$600 l of tap water so that the fluid height at rest above the bottom plate is of $\sim$58 cm. It is closed by a Plexiglas top lid. (b) Experimental set-up in solid body rotation at 75 RPM, with the side green laser turned on. The difference in fluid height between the centre of the tank and its border is of $\sim$76 cm and the fluid height at the centre is $h_{min}=20$ cm. (c) View of the bottom plate through which the forcing is performed. The plate has the shape of a curly bracket for the fluid height to increase exponentially with the radius, see (2.3). It is drilled with 128 holes corresponding to 64 inlets and 64 outlets connected to six submersible pumps. (d) View of the six pumps and 128 hoses placed beneath the bottom plate.

Figure 2

Figure 3. Instantaneous velocity fields computed from PIV measurements in the statistically stationary state reached in the two experimental regimes. The shaded areas in the top-right and bottom-left corners are shadow areas due to the laser refraction: no measurements are performed in these areas. The colours represent the vertical component of the vorticity $\zeta$. Note that there is a factor ten between the colour scales in the two panels. (a) Regime I: velocity field obtained at time $t=24~\min = 1800$$t_R$ and averaged over 1 s. (b) Regime II: velocity field obtained at time $t=19\ \min = 1425$$t_R$ and averaged over 1 s.

Figure 3

Figure 4. Zonal flow and zonal mean potential vorticity in the two experimental regimes represented in figures 3 and 5. (a–c) Regime I. (a) Space–time diagram showing the evolution of the instantaneous zonal flow radial profile $\langle u_\phi \rangle _\phi (\rho ,t)$ during the experiment. Dotted lines: location of the forcing rings. (b) Symbols: instantaneous zonal flow at time $t=2500\ t_R$. Black line: time-averaged zonal flow $\overline {\langle u_\phi \rangle _\phi }(\rho )$ from $t=1500$ to 3000 $t_R$. Dotted lines: location of the forcing rings. (c) Symbols: potential vorticity instantaneous profile at time $t=2500\ t_R$. Grey line: initial potential vorticity profile (hidden behind the symbols). (d–f) Regime II (the same quantities are plotted).

Figure 4

Figure 5. Instantaneous maps in regime I (a–c) and II (d–f ). The black circle marks the tank boundary, and the shaded areas are the shadows where no measurements can be performed. The dashed curves in the top-left quadrant of each subplot represent the forcing rings location. (a–c) Regime I at time $t=24 \ \min = 1800$$t_R$ and averaged over 1 s. (a) Azimuthal component of the velocity $u_\phi$. (b) Radial component of the velocity $u_\rho$. (c) Vertical component of the vorticity $\zeta$. (d–f ) Regime II at time $t=19\ \min = 1425$$t_R$ and averaged over 1 s. (d) $u_\phi$. (e) $u_\rho$. (f) $\zeta$. Note the different colour scales for the two regimes.

Figure 5

Table 1. Typical instantaneous RMS velocity (3.1), Rossby and Reynolds global and local numbers. Here $R$ is the tank's inner radius $R=0.49$ m, and $f = 2\varOmega = 15.7\ \textrm {rad}\ \textrm {s}^{-1}$. For the local Rossby and Reynolds numbers, we use the distance between two forcing rings as a length scale, $\ell =7.3$ cm. Note that these values correspond to two typical experiments, but may vary in each regime depending on the forcing amplitude.

Figure 6

Figure 6. Experiment illustrating the bistability between regimes I and II: the forcing is initially of low amplitude and stationary, so that we start in regime I ($P_i=\{14,20,46,72,100,100\}\,\%$, $U_f=3.3 \times 10^{-3}\ \mathrm {m}\ \mathrm {s}^{-1}$). At $t=360\ t_R$, a finite perturbation is created by varying the third forcing ring power randomly around its initial value, leading to the transition to regime II ($P_i=\{14,20,46\pm 20,72,100,100\}\,\%$). At $t=1600\ t_R$, the forcing is set back to its initial state but the flow remains in regime II. At time $t=2250\ t_R$, a second finite-amplitude perturbation is performed ($P_i=\{14,20,46,72\pm 20,100,100\}\,\%$) (a). Hovmöller plot: zonal flow profile as a function of time. (b) Total ($\mathcal {K}$), zonal ($\mathcal {K}_z$) and fluctuating ($\mathcal {K}_f$) kinetic energy as a function of time.

Figure 7

Figure 7. (a) Experimental hysteresis loop. The time-averaged RMS velocity of the flow $\bar {u}^{\textit{RMS}}$ (3.5) is plotted as a function of the forcing amplitude $U_f$ (see appendix B). The top and right axes correspond to associated non-dimensional quantities. On the right axis, we use the Reynolds number based on the mean flow RMS velocity, $\overline {Re}=\bar {u}^{\textit{RMS}}\ell /\nu$ ($\ell =7.3\ \textrm {cm}$ is the distance between two forcing rings). For the top axis, we use the typical velocity expected at the transition $U_t$ (see § 4.4 and (4.34)). For each curve, the forcing is either increased (reddish) or decreased (bluish) step by step. The different colours are different experiments. The shaded area is the bistable zone. The grey points in regime II correspond to experiments initialized with the exact same forcing and for which saturation leads to three possible jets configurations represented in panel (b). The last point of the yellow curve is in configuration 2, but may not have reached its stationary state. (b) Time-averaged zonal velocity maps in regime I and II. In regime II multiple steady states can be obtained for the same forcing. The configurations 1, 2, 3 correspond to the points labelled accordingly in panel (a).

Figure 8

Figure 8. Evolution of the total kinetic energy $\mathcal {K}$ during transitions from regime $\textrm {I} \rightarrow \textrm {II}$ (red curves) and $\textrm {II} \rightarrow \textrm {I}$ (blue curves). The normalized total kinetic energy is plotted as a function of time in units of rotation period. (a) Qualitative location of the transitions on the hysteresis loop. (b) Transitions from $\textrm {II}\rightarrow \textrm {I}$. The time is initialized at the moment when the forcing was changed from a super-critical one to a subcritical one. The normalized kinetic energy decays on a time scale $\tau$ obtained from an exponential fit (lines). (c) Transitions from $\textrm {I}\rightarrow \textrm {II}$, starting from the same initial state.

Figure 9

Figure 9. Comparison between the experimental flow and the linear QG model. (a–d) Experimental flow measured 2 s after the third forcing was turned on. The experimental data, originally obtained in a cylindrical geometry, is remapped for the sake of comparison with our cartesian model. Here $R_3$ is the radius of the third forcing ring. Only eight vortices are visualized, but the third ring contains 18 vortices. (e–h) Solution of the linear model (4.17) at time $t=$ 2 s. The model parameters ($\alpha$, $\beta$, $q_m$, $k_f$ and $U$) are estimated from the experimental parameters. (a,e) Zonal velocity perturbation. (b,f) Radial velocity perturbation (note that $u_\rho$ should be compared with $-v$). (c,g) Vorticity. (d,h) Reynolds stresses divergence (zonal flow acceleration).

Figure 10

Figure 10. Comparison of the Reynolds stresses divergence between the experiment and the linear model solution. (a) Experimental Reynolds stresses divergence (4.8). (b) Reynolds stresses divergence computed from the linear model (4.19). Both the experiment and the linear model show the generation of a prograde jet at the forcing location, flanked with two retrograde jets.

Figure 11

Figure 11. (a) Streamfunction amplitude as a function of the background zonal flow $U$. Each symbol is a solution of the linear model with a different background zonal flow. The black line is the corresponding analytical amplitude in the case of a doubly periodic forcing (4.23). (b) Reynolds stresses at $y=0$ as a function of the background zonal flow $U$. Each symbol is a solution of the linear model with a different background zonal flow. The black line represents the best fit of the Lorentzian given by (4.27) where the amplitude $\mathcal {R}_m$ is a free parameter. In both panels, the vertical dashed black line shows the location of $U=-c$, where $c$ is the forced Rossby wave phase speed (4.24).

Figure 12

Figure 12. Visualization of the stationary solutions ($U_1,U_2,U_3$) of the zonal flow evolution equation (4.28). Except the forcing amplitude, all the parameters are fixed and equal to the experimental parameters ($\alpha = 5.6\times 10^{-3}\ \mathrm {s}^{-1}$, $k_f=l_f= 63\ \mathrm {rad}\ \mathrm {m}^{-1}$, $c=6.3\times 10^{-3}\ \mathrm {m}\ \mathrm {s}^{-1}$, $\gamma ^{2}=1.99\times 10^{-4}$). (a) Illustrative case of a small forcing amplitude $\mathcal {R}_m < \mathcal {R}_{1}$ and a small friction or a too high friction. Note that $U_1$ is very small, but not zero. (b) Illustrative case of a forcing in the range $\mathcal {R}_m \in [\mathcal {R}_{1}, \mathcal {R}_{2}]$ and a small friction. (c) Illustrative case of a high forcing amplitude $\mathcal {R}_m > \mathcal {R}_{2}$ and a small friction. (d) Amplitude of the three stationary solutions as a function of the forcing amplitude $\mathcal {R}_m$. The black dots represent the unstable solution whereas the white ones are stable. The shaded area is the bistable range, bounded by $\mathcal {R}_1$ and $\mathcal {R}_2$ (4.31).

Figure 13

Figure 13. Rossby waves excited by the forcing. The third forcing ring ($R_3=0.214$ m) is turned on at its maximum power from time $t=0$ to 75 $t_R$. (a) Time evolution of the radial component of the velocity at a fixed radius $\rho =0.17$ m. (b) Same data band-passed filtered between 0.06 and 0.12 Hz. The slope of the dashed line is the non-Doppler-shifted phase speed of the Rossby waves excited by the forcing (4.24) $c \approx -6.3\ \mathrm {mm}\ \textrm {s}^{-1}$. The slope of the full line is the Doppler-shifted phase speed $\langle u_\phi \rangle _\phi + c$. It increases in absolute value since the zonal flow increases when the forcing is turned on, and at the chosen radius the flow is retrograde, as represented on the top panel.

Figure 14

Figure 14. Illustration of the jet's instability for an experiment in regime II ($U_f=3.3\ \mathrm {mm} \ \mathrm {s^{-}1}$): (a) $t=2412$ to $2436\ t_R$; (b) $t=2486$ to $2511\ t_R$; (c) $t=2568$ to $2580\ t_R$; (d) $t=2580$ to $2593\ t_R$; (e) $t=2593$ to $2605\ t_R$. This sequence is also available as supplementary movie 5.

Figure 15

Figure 15. Calibration of the experimental forcing. Left to right and top to bottom: rings C1 to C6. The total RMS velocity inside of a region of interest is plotted for each pump separately, and several fractions of the pump maximum power (dots). The lines are the result of a linear fit between the induced velocity and the pump power.

Figure 16

Figure 16. Sensitivity of the width of the bistable zone (left) and the zonal flow amplitude at the transition (right) to the model parameters. Here $\mathcal {R}_1$ and $\mathcal {R}_2$ are respectively the lower and upper limits of the bistable zone, in terms of forcing amplitude (see figure 12); $U_{1,max}$ and $U_{3,min}$ are the zonal flow amplitude at the saddle-node bifurcation $S_2$ and $S_1$, respectively (figure 12). (a) Varying friction coefficient $\alpha$. The vertical dashed line shows the experimental friction. (b) Varying forcing wavenumber $k_f$. The horizontal dashed lines show the mean flow amplitude at the transitions measured experimentally. (c) Varying $\beta$ parameter. The vertical dashed line shows the experimental $\beta$.

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