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Experimental study of the convection in a rotating tangent cylinder

Published online by Cambridge University Press:  21 March 2018

Kélig Aujogue*
Affiliation:
Applied Mathematics Research Centre, Coventry University, Priory Street, Coventry CV15FB, UK
Alban Pothérat
Affiliation:
Applied Mathematics Research Centre, Coventry University, Priory Street, Coventry CV15FB, UK
Binod Sreenivasan
Affiliation:
Centre for Earth Sciences, Indian Institute of Science, Bangalore 560 012, India
François Debray
Affiliation:
Laboratoire National des Champs Magnétiques Intenses-Grenoble, CNRS/UGA-UPS-INSA, France
*
†Email address for correspondence: aujogue.kelig@gmail.com

Abstract

This paper experimentally investigates the convection in a rapidly rotating tangent cylinder (TC), for Ekman numbers down to $E=3.36\times 10^{-6}$. The apparatus consists of a hemispherical fluid vessel heated in its centre by a protruding heating element of cylindrical shape. The resulting convection that develops above the heater, i.e. within the TC, is shown to set in for critical Rayleigh numbers and wavenumbers respectively scaling as $Ra_{c}\sim E^{-4/3}$ and $a_{c}\sim E^{-1/3}$ with the Ekman number $E$. Although exhibiting the same exponents as for plane rotating convection, these laws reflect much larger convective plumes at onset. The structure and dynamics of supercritical plumes are in fact closer to those found in solid rotating cylinders heated from below, suggesting that the confinement within the TC induced by the Taylor–Proudman constraint influences convection in a similar way as solid walls would do. There is a further similarity in that the critical modes in the TC all exhibit a slow retrograde precession at onset. In supercritical regimes, the precession evolves into a thermal wind with a complex structure featuring retrograde rotation at high latitude and either prograde or retrograde rotation at low latitude (close to the heater), depending on the criticality and the Ekman number. The intensity of the thermal wind measured by the Rossby number $Ro$ scales as $Ro\simeq 5.33(Ra_{q}^{\ast })^{0.51}$ with the Rayleigh number based on the heat flux $Ra_{q}^{\ast }\in [10^{-9},10^{-6}]$. This scaling is in agreement with heuristic predictions and previous experiments where the thermal wind is determined by the azimuthal curl of the balance between the Coriolis force and buoyancy. Within the range $Ra\in [2\times 10^{7},10^{9}]$ which we explored, we also observe a transition in the heat transfer through the TC from a diffusivity-free regime where $Nu\simeq 0.38E^{2}Ra^{1.58}$ to a rotation-independent regime where $Nu\simeq 0.2Ra^{0.33}$.

Information

Type
JFM Papers
Copyright
© 2018 Cambridge University Press 
Figure 0

Figure 1. Schematic representation of the Earth’s interior. This paper focuses on the north part of the region inside the tangent cylinder represented in green.

Figure 1

Figure 2. (a) Vertical cross-section of the experimental geometry with $T_{H}$ the temperature at the heater, $T_{D}$ the temperature at the dome, $\unicode[STIX]{x1D6FA}$ the rotation speed, $g$ being the gravity and $F$ the heat flux through the heater. The green dashed lines represent the two horizontal PIV planes. The red line is the surface of the heater. The blue line is the surface of the dome. The dashed/dotted black line is the axis of symmetry and rotation of the experiment. The dotted lines are the lateral boundary of the tangent cylinder. (b) Technical sketch of LEE, 1. liquid heater 2. dome 3. cooling water 4. K-type thermocouples connected under and in the ceramic plate 5. mirror 6. torque tube 7. pipe carrying ethylene glycol 8. enclosure for LASER, mirror and optical elements. (Material partially presented in Aujogue et al. (2016).)

Figure 2

Table 1. Range of achievable parameters in the experiment and comparison with the apparatus and Earth’s core parameters of Aurnou et al. (2003). Here $\unicode[STIX]{x1D708}$ is the viscosity, $\unicode[STIX]{x1D6FA}$ the rotation rate, $d$ is the height of fluid above the centre of the heater, $g$ the gravitational constant, $\unicode[STIX]{x1D6FC}$ the thermal expansion coefficient, $\unicode[STIX]{x0394}T$ the temperature difference between the heater and the dome, $\unicode[STIX]{x1D705}$ the thermal diffusivity, $D_{D}$ the diameter of the dome and $D$ the diameter of the heater. Note that the values of $Ra$ for the Earth are highly uncertain (Schubert & Soderlund 2011). (Material originally presented in Aujogue et al. (2016).) Values of $\unicode[STIX]{x1D6FA}$, $\unicode[STIX]{x0394}T$ and $Fr$ were not provided in Aurnou et al. (2003) and have been calculated from dimensional and non-dimenisonal parameters available in this paper.

Figure 3

Figure 3. Critical Rayleigh number $Ra_{c}$ and critical wavenumber $a_{c}=2\unicode[STIX]{x03C0}R/r_{0}$ at onset versus the Ekman number $E$ for three geometries: present case (symbols and dotted lines), infinite plane layer (solid lines) and wall modes in a finite cylinder obtained from the theory of Zhang & Liao (2009) ((3.3) and (3.4)), dashed lines). Raw and interpolation data for this figure are available as the supplementary material at https://doi.org/10.1017/jfm.2018.77.

Figure 4

Figure 4. Average over time of the vertical component of velocity from PIV measurement above the liquid heater at the onset of convection. The averaging time is 15 times smaller than the precession time scale $\unicode[STIX]{x1D70F}_{p}=2\unicode[STIX]{x03C0}/\unicode[STIX]{x1D714}_{p}$. Velocities are normalised by the maximum velocity of the flow. Here $z$ and $r$ are normalised by the maximum height above the heater and the radius of the heater respectively. The blue line represents the inner boundary of the glass dome. The red arrows point to the position of the TC. (a) $E=2.51\times 10^{-5}$ and $Ra=3.48\times 10^{7}$. (b) $E=3.36\times 10^{-6}$ and $Ra=3.82\times 10^{8}$.

Figure 5

Figure 5. Time-averaged velocity fields (arrows) with vorticity field (colour bar) in the horizontal plane at $z/d=3/4$ for different Rayleigh numbers with $E=1.15\times 10^{-5}$. The blue line represents the boundary of the glass dome. The red line represents the position of the heater that defines the TC. Wall modes can be identified where vorticity extrema are present near the boundary of the TC (e.g. a,c). The averaging time is 15 times smaller than the precession time scale $\unicode[STIX]{x1D70F}_{p}=2\unicode[STIX]{x03C0}/\unicode[STIX]{x1D714}_{p}$. (a) $R_{c}=0.13$, fast wall mode (WM) at onset. (b) $R_{c}=1.26$, quasi-geostrophic (QG) mode. (c) $R_{c}=3.58$, QG and WM interaction. (d) $R_{c}=6.29$, merging of centre modes. (e) $R_{c}=8.25$, merging of centre modes. (f) $R_{c}=11.27$, central retrograde vortex.

Figure 6

Figure 6. Time-averaged velocity fields (arrows) with vorticity field (colour bar) in the horizontal plane at $z/d=3/4$ for different Rayleigh numbers with $E=6.36\times 10^{-6}$. The blue line represents the boundary of the glass dome. The red line represents the position of the heater that defines the TC. Wall modes can be identified where vorticity extrema are present near the boundary of the TC (e.g. c). The averaging time is 15 times smaller than the precession time scale $\unicode[STIX]{x1D70F}_{p}=2\unicode[STIX]{x03C0}/\unicode[STIX]{x1D714}_{p}$. (a) $R_{c}=0.35$, localised structure near the centre at onset. (b) $R_{c}=1.26$, modulated modes. (c) $R_{c}=2.32$, interaction between wall modes and centre modes. (d) $R_{c}=4.40$, merging of centre modes. (e) $R_{c}=8.17$, merging of centre modes. (f) $R_{c}=11.91$, central retrograde vortex.

Figure 7

Figure 7. Evolution of the precession $\unicode[STIX]{x1D714}_{p}$ and the wavenumber $a$ as function of the degree of criticality. Raw and interpolation data for this figure are available as the supplementary material.

Figure 8

Figure 8. Variations of the Nusselt number $Nu$ emphasising the scaling $Nu/E^{2}\simeq 0.2Ra^{0.33}$ for large Rayleigh numbers (a) and the scaling $Nu\simeq 0.38E^{2}Ra^{1.58}$ at moderate Rayleigh numbers (b). Raw and interpolation data for this figure are available as the supplementary material.

Figure 9

Figure 9. Variations of $Nu^{\ast }$ with $Ra_{q}^{\ast }$. Raw and interpolation data for this figure are available as the supplementary material.

Figure 10

Figure 10. Azimuthally and time-averaged radial profiles of azimuthal velocities $\langle u_{\unicode[STIX]{x1D703}}\rangle _{\unicode[STIX]{x1D703}t}(r)$, for several levels of criticality. (a,b) Data from horizontal plane at $51.5^{\circ }$. (c,d) Data from horizontal plane at $20^{\circ }$. (a,c) $E=1.15\times 10^{-5}$, (b,d) $E=6.36\times 10^{-6}$. Vertical dashed line: TC boundary, vertical solid line: position of the glass dome.

Figure 11

Figure 11. Variations of the Rossby number Scaling $Ro$ with $Ra_{q}^{\ast }$. Raw and interpolation data for this figure are available as the supplementary material.

Figure 12

Figure 12. (a,c) $\langle \sqrt{\langle u_{z}(r)^{2}\rangle _{z}}\rangle _{t}$ (top) and $\langle \sqrt{\langle u_{r}(r)_{r}^{2}\rangle _{z}}\rangle _{t}$ (bottom) for several increments of supercriticality and $E=1.15\times 10^{-5}$. (b,d) Similarly, $\langle \sqrt{\langle u_{z}(r)\rangle _{z}^{2}}\rangle _{t}$ and $\langle \sqrt{\langle u_{r}(r)_{r}^{2}\rangle _{z}}\rangle _{t}$ for several increments of supercriticality and $E=6.36\times 10^{-6}$.

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