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Onset of turbulence and layering in stratified columnar Taylor–Green vortices

Published online by Cambridge University Press:  06 August 2025

Junwei Guo
Affiliation:
Department of Civil Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada
John R. Taylor
Affiliation:
Department of Applied Mathematics and Theoretical Physics, Centre for Mathematical Sciences, University of Cambridge, Wilberforce Road, Cambridge CB3 0WA, UK
Qi Zhou*
Affiliation:
Department of Civil Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada
*
Corresponding author: Qi Zhou, qi.zhou1@ucalgary.ca

Abstract

We use direct numerical simulations to examine the onset of stratified turbulence triggered by the zigzag instability recently identified in columnar Taylor–Green vortices (Guo et al. 2024, J. Fluid Mech., vol. 997, A34) and its role in layer formation within the flow. The study focuses on Froude numbers $0.125 \leqslant \textit{Fr} \leqslant 2.0$ and Reynolds numbers ${\textit{Re}}$ ranging from 800 to 3200. The breakdown of the freely evolving vortex array is driven by local density overturns, combining shear and convective mechanisms initiated by the primary zigzag instability. Our results show a linear relationship between the peak buoyancy Reynolds number ${{\textit{Re}}}_b^{\star }$, driven by the zigzag instability, and ${\textit{Re}}\, {\textit{Fr}}^2$. When the flow does not exhibit local shear or convective instability, the value of ${{\textit{Re}}}_b^{\star }$ falls below unity. Both density and momentum layers arise from the zigzag instability: horizontal velocity layers are strong and persistent, while density layers are weaker and more transient. The vertical scale of the mean shear layers increases with ${\textit{Fr}}$ for ${\textit{Fr}} \leqslant 1$, shows weak dependence on ${\textit{Re}}$, and agrees well with the length scale associated with the fastest-growing linear mode of the zigzag instability. Further analysis in the sorted buoyancy coordinate highlights the role of density overturns caused by the zigzag instability in forming buoyancy layers during the transition to turbulence.

Information

Type
JFM Papers
Creative Commons
Creative Common License - CCCreative Common License - BYCreative Common License - NCCreative Common License - ND
This is an Open Access article, distributed under the terms of the Creative Commons Attribution-NonCommercial-NoDerivatives licence (https://creativecommons.org/licenses/by-nc-nd/4.0/), which permits non-commercial re-use, distribution, and reproduction in any medium, provided that no alterations are made and the original article is properly cited. The written permission of Cambridge University Press must be obtained prior to any commercial use and/or adaptation of the article.
Copyright
© The Author(s), 2025. Published by Cambridge University Press
Figure 0

Table 1. Summary of DNS parameters: $(N_x,N_y,N_z)$ are the numbers of grid points used in each direction, $h$ is the grid spacing, $\eta _{\textit{min}}$ is the minimum Kolmogorov scale at peak dissipation, $\Delta t$ is the time step size, ${\textit{Re}}_b^\star$ is the peak value of the buoyancy Reynolds number, and ${\textit{Fr}}_t^\star$ is the maximum turbulent Froude number. Both ${\textit{Re}}_b^\star$ and ${\textit{Fr}}_t^\star$ are discussed in § 3.2.

Figure 1

Figure 1. Volume-rendering images of the vertical vorticity field $\omega _z=\partial v/ \partial x- \partial u/ \partial y$, from the DNS with ${\textit{Re}}=1600$ and ${\textit{Fr}}=1.0$. The first image in the sequence was captured at time $t=36$. Subsequent images are spaced at regular intervals of 4.0 units of time, arranged from left to right and top to bottom. An animation of the flow evolution can be found as movie 1 in the supplementary movies available at https://doi.org/10.1017/jfm.2025.10420.

Figure 2

Figure 2. Time series of (a,b) kinetic energy components and (c) dissipation rate for the case with ${\textit{Re}}=1600$ and ${\textit{Fr}} = 1.0$. Circles in (b,c) correspond to $t=40$, 44 and 48.

Figure 3

Figure 3. A 3-D visualisation of the onset of turbulence in a columnar TG vortex array (${\textit{Re}}=1600$, ${\textit{Fr}} = 1.0$). The red and blue surfaces represent isosurfaces of vertical vorticity $\omega _z = 0.75$ (red) and $\omega _z = -0.75$ (blue). Convectively unstable regions, where $\partial \rho _{\textit{tot}} / \partial z \gt 0$, are highlighted in dark green. The snapshots are shown at times (a) $t = 4$, (b) $t = 40$, (c) $t = 44$ and (d) $t = 48$.

Figure 4

Figure 4. Visualisation of $x$$z$ transects showing (a) the vertical vorticity $\omega _z$, (b) the vertical gradient of $\rho _{\textit{tot}}$, (c) the vertical velocity $w$, and (d) the horizontal velocity $u$ for the case with ${\textit{Re}}=1600, \textit{Fr} = 1.0$. The transects are taken along $y=\unicode{x03C0} /2$, as indicated by the red dashed lines in figure 3(a). Black solid lines represent isopycnals, spaced at intervals $\Delta \rho _{\textit{tot}}=1/3$. Snapshots are shown for times $t=40$, $44$ and $48$.

Figure 5

Figure 5. (a) Streamlines (represented by solid lines with arrows) at $y=\unicode{x03C0} /2$ for the case with ${\textit{Re}}=1600$ and ${\textit{Fr}}=1.0$. (b) A zoomed-in view of the region outlined by the blue box in (a). Red solid lines represent isopycnals, spaced at intervals $\Delta \rho _{\textit{tot}}=0.16$.

Figure 6

Figure 6. Schematic illustrating the overturning mechanism. Arrows represent the fluid velocity, while the lines correspond to two isopycnal surfaces located above and below the neutral plane where $w=0$. The heights of neutral planes are marked by grey dashed lines. Time progresses from left to right.

Figure 7

Figure 7. Volume-rendering images of (a) the vorticity component $\omega _y$, and (b) the normal strain rate $\partial v/\partial y$, both along the $y$-axis, for the case with ${\textit{Re}} = 1600$ and ${\textit{Fr}} = 1.0$ at $t = 40$. The green arrows indicate the overturning billows highlighted in figure 3(d).

Figure 8

Figure 8. Sample scatter plots of squared vertical shear $S^2$ versus vertical density gradient $\partial \rho _{\textit{tot}}/\partial z$ for times corresponding to the snapshots in figure 3. The colour scale is adjusted to display only points where $\widehat {{\textit{Re}}_b} \geqslant 1$. The dotted vertical line indicates $\partial \rho _{\textit{tot}}/\partial z = -1$, and the dashed horizontal line marks $S^2 = 4/{\textit{Fr}}^2$, corresponding to the shear strength required for the gradient Richardson number to reach $1/4$ under background uniform stratification. Regions I, II and III, as labelled in (a), delineate different potential instability mechanisms: regions I and II correspond to strong shear ($S^2 \gt 4/{\textit{Fr}}^2$), while regions II and III correspond to weakened (or even reversed) vertical density gradient from the background value ($\partial \rho _{\textit{tot}}/\partial z \gt -1$).

Figure 9

Figure 9. Volume fraction of (a) convectively unstable regions ($\partial \rho _{\textit{tot}} /\partial z \gt 0$) and (b) shear unstable regions ($Ri \lt 1/4$), sampled at the time of peak volume-averaged dissipation rate, as functions of the maximum buoyancy Reynolds number ${\textit{Re}}_b^\star$. The dotted lines represent a linear fit between $\log {\textit{Re}}_b^\star$ and the volume fractions.

Figure 10

Figure 10. Maximum buoyancy Reynolds number ${\textit{Re}}_b^\star$ versus ${\textit{Re}}\, {\textit{Fr}}^2$ for all cases simulated.

Figure 11

Figure 11. Maximum turbulent Froude number ${\textit{Fr}}_t^\star$ versus (a) ${\textit{Fr}}$ and (b) ${\textit{Re}}_b^\star$ for all cases simulated.

Figure 12

Figure 12. Volume-rendering images of the horizontal velocity $u$ from the DNS with ${\textit{Re}}=1600$ and $Fr=1.0$. The images are shown at (a) $t=48$, (b) $t=56$, (c) $t=64$ and (d) $t=72$. An animation of the flow evolution can be found as movie 2 in the supplementary material.

Figure 13

Figure 13. Visualisation of $x$$z$ transects showing (a) the horizontal velocity $u$, and (b) the density perturbation $\rho$, for the case with ${\textit{Re}}=1600, \textit{Fr} = 1.0$. The transects are taken along $y=\unicode{x03C0} /2$, as indicated by the red dashed lines in figure 3(a). Snapshots are shown for times $t=48$, $56$, $64$ and $72$.

Figure 14

Figure 14. Horizontally averaged velocity $\langle u \rangle _h$ as a function of time $t$ and vertical position $z$. Each column corresponds to a different Froude number, from left to right: $Fr = 0.25$, $0.5$, $1.0$ and $2.0$. Each row represents a different Reynolds number: (a) ${\textit{Re}} = 800$, (b) $Re=1600$, and (c) $Re=3200$.

Figure 15

Figure 15. The average vertical wavenumber $\tilde {k}$ representing the horizontally averaged mean flow, $\langle u \rangle _h$, as a function of (a) ${\textit{Re}}$, and (b) ${\textit{Fr}}$.

Figure 16

Figure 16. The time-averaged mean vertical wavenumber $\tilde {k}$ representing the horizontally averaged velocity $\langle u \rangle _h$ observed in the DNS, versus the fastest-growing wavenumber $k_{\textit{fgm}}$, according to the LSA.

Figure 17

Figure 17. Same layout as in figure 14, but showing the horizontally averaged density perturbation $\langle \rho \rangle _h$.

Figure 18

Figure 18. (a) The sorted buoyancy gradient $N^2_*$, and (b) the scaled effective diffusivity $\kappa _e/\kappa$ as they vary in the tracer-based, sorted coordinate $z_*$ and time for the case $({\textit{Re}},Fr)=(1600,1.0)$.

Figure 19

Figure 19. Plots of (a) $N^2_*$ and (b) $\kappa _e\, Pr$ as functions of $z_*$ at various times for the case $({\textit{Re}},Fr)=(1600,1.0)$.

Supplementary material: File

Guo et al. supplementary movie 1

Movie 1: Animation of the vertical vorticity field that corresponds to the snapshots shown in figure 1.
Download Guo et al. supplementary movie 1(File)
File 6.8 MB
Supplementary material: File

Guo et al. supplementary movie 2

Movie 2: Animation of the horizontal velocity field that corresponds to the snapshots shown in figure 12.
Download Guo et al. supplementary movie 2(File)
File 7.8 MB