Hostname: page-component-6898cfcb55-cbk24 Total loading time: 0 Render date: 2026-11-11T08:07:56.725Z Has data issue: false hasContentIssue false

On the coupling between spin-up and aspect ratio of vortices in rotating stratified flows: a predictive model

Published online by Cambridge University Press:  20 July 2015

Marius Ungarish*
Affiliation:
Department of Computer Science, Technion, Haifa 32000, Israel
*
†Email address for correspondence: unga@cs.technion.ac.il

Abstract

We consider the long-time (many revolutions) behaviour of an axisymmetric isolated anticyclonic vortex of constant density which floats inside a large ambient linear-stratified fluid rotating with constant ${\it\Omega}$ . We have developed a closed simple model for the prediction of the vertical thickness to diameter aspect ratio ${\it\alpha}$ (and actually the shape) and internal angular velocity ${\it\omega}$ , relative to the ambient, as functions of time $t$ . (In our model ${\it\omega}$ is scaled with ${\it\Omega}$ ; the literature sometimes uses the Rossby number $Ro={\it\omega}/2$ .) This model is an extension of the model of Aubert et al. (J. Fluid Mech., vol. 706, 2012, pp. 34–45) and Hassanzadeh et al. (J. Fluid Mech., vol. 706, 2012, pp. 46–57), which derived the connection between ${\it\alpha}$ and ${\it\omega}$ , for prescribed $f=2{\it\Omega}$ and buoyancy frequency of the ambient $\mathscr{N}$ . This work adds the balance of angular momentum and resolves the spin-up process of the vortex, which were not accounted for in the previous model. The Ekman number $E={\it\nu}/({\it\Omega}L^{2})$ now enters into the formulation; here ${\it\nu}$ is the coefficient of kinematic viscosity and $L$ is the half-height of the vortex, roughly (a sharper definition is given in the paper). The model can be applied to cases of both fixed-volume and injection-sustained vortices.

The often-cited aspect ratio ${\it\alpha}=0.5f/\mathscr{N}$ corresponds to ${\it\omega}\approx -1$ , which is a plausible initial condition for typical systems. We show that the continuous ‘decay’ of ${\it\alpha}$ from that value over many revolutions of the system is indeed governed by the spin-up effect which reduces $|{\it\omega}|$ , but with significant differences to the classical spin-up of a fluid in a closed solid container. The spin-up shear torque decays with time because the thickness of the boundary shear layer increases. The layer starts as a double Ekman layer (between two fluids) but it quite quickly expands due to stratification effects, and later due to viscous diffusion. This prolongs the spin-up somewhat beyond the classical $E^{-1/2}/{\it\Omega}$ time interval. Moreover, when $|{\it\omega}|$ becomes small, the momentum of angular inertia of the vortex increases like $(1+(1/3)|{\it\omega}|^{-1})$ ; this further hinders the spin-up, and prolongs the process.

Comparisons of the prediction of the model with previously published experimental and Navier–Stokes simulation data were performed for four cases. In three cases the agreement is good. In one case, the model predicts a much faster decay than the observed one; we have suggested a plausible explanation for this discrepancy.

Information

Type
Papers
Copyright
© 2015 Cambridge University Press 
Figure 0

Figure 1.The vortex shape according to the ALM12 and HML12 model at three times, $t_{0}, assuming ${\it\omega}(t_{i})=-1,-0.2,-0.01$. $R(0)$ is the radius at $t_{0}$. The half-thickness $h$ is scaled with $R(0)\,f/\!\mathscr{N}$.

Figure 1

Figure 2.Schematic description of the spin-up flow. The interface of the vortex (upper half) is shown by the thick (black) curve. The domain between the thin lines is the ‘boundary layer’ ${\it\delta}$ in which transition of ${\it\omega}$ occurs. The density is ${\it\rho}_{c}$ (constant) inside the vortex, and ${\it\rho}_{c}(1-{\it\sigma}z)$ in the ambient fluid. $\mathscr{N}^{2}={\it\sigma}g$.

Figure 2

Figure 3.Comparison with fixed-volume experiment of ALM12: ${\it\alpha}\mathscr{N}\!/f$ as a function of $t/T$ (number of revolutions, where $T=2{\rm\pi}/{\it\Omega}$). The thick solid line shows the model prediction, the symbols joined by the thin line are experimental data, $f=6.8~\text{s}^{-1},\mathscr{N}=1.6~\text{s}^{-1}$. The model uses $f/\!\mathscr{N}=4.25$, $E=5.1\times 10^{-5}$, ${\it\omega}(0)=-0.95$.

Figure 3

Figure 4.Comparison with fixed-volume Navier–Stokes simulation of HML12: ${\it\alpha}\mathscr{N}\!/f$ as a function of $t/T$. The thick solid line shows the model, the symbols joined by the thin line are the simulation data. The model uses $f/\!\mathscr{N}=5$, $E=7.7\times 10^{-5}$, ${\it\omega}(0)=-0.40$.

Figure 4

Figure 5.Comparison with experiment of Hedstrom & Armi (1988): ${\it\alpha}\mathscr{N}/f$ as a function of $t/T$. Injection stops at $t/T=40$. The thick solid line shows the model prediction, the symbols (joined by the thin line) are the experiment; the triangles denote an unstable domain. The model uses $f/\!\mathscr{N}=1.88$; $E$ decreases with time, from $1.3\times 10^{-2}$ at $t/T=3$ to $2.3\times 10^{-4}$ at $t/T\geqslant 40$.

Figure 5

Figure 6.Comparison with experiment of ALM12: ${\it\alpha}\mathscr{N}\!/f$ as a function of $t/T$. Injection active all time. The thick solid line shows the model prediction, the symbols show the experimental data. The model uses $f/\!\mathscr{N}=0.70$; $E$ decreases with time, from $3.9\times 10^{-2}$ at $t/T=3$ to $4.1\times 10^{-3}$ at $t/T=100$.