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Internal heating profiles for which downward conduction is impossible

Published online by Cambridge University Press:  17 September 2024

Ali Arslan*
Affiliation:
Institute of Geophysics, ETH Zürich, Zürich 8092, Switzerland
Giovanni Fantuzzi
Affiliation:
Department of Mathematics, FAU Erlangen-Nürnberg, Erlangen 91058, Germany
John Craske
Affiliation:
Department of Civil and Environmental Engineering, Imperial College London, London SW7 2AZ, UK
Andrew Wynn
Affiliation:
Department of Aeronautics, Imperial College London, London SW7 2AZ, UK
*
Email address for correspondence: ali.arslan@eaps.ethz.ch

Abstract

We consider an internally heated fluid between parallel plates with fixed thermal fluxes. For a large class of heat sources that vary in the direction of gravity, we prove that $\smash { \smash {{\langle {\delta T} \rangle _h}} } \geq \sigma R^{-1/3} - \mu$, where $\smash { \smash {{\langle {\delta T} \rangle _h}} }$ is the average temperature difference between the bottom and top plates, $R$ is a ‘flux’ Rayleigh number and the constants $\sigma,\mu >0$ depend on the geometric properties of the internal heating. This result implies that mean downward conduction (for which $\smash { \smash {{\langle {\delta T} \rangle _h}} }< 0$) is impossible for a range of Rayleigh numbers smaller than a critical value $R_0:=(\sigma /\mu )^{3}$. The bound demonstrates that $R_0$ depends on the heating distribution and can be made arbitrarily large by concentrating the heating near the bottom plate. However, for any given fixed heating profile of the class we consider, the corresponding value of $R_0$ is always finite. This points to a fundamental difference between internally heated convection and its limiting case of Rayleigh–Bénard convection with fixed-flux boundary conditions, for which $\smash {{\langle {\delta T} \rangle _h}}$ is known to be positive for all $R$.

Information

Type
JFM Papers
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
Copyright
© The Author(s), 2024. Published by Cambridge University Press.
Figure 0

Figure 1. (a) Internally heated and (b) RBC with fixed-flux boundaries, where $H(z)$ is a positive non-uniform heating profile. In both panels, the red dashed line denotes the conductive temperature profiles and the red solid line the mean temperature profiles in the turbulent regime. In (a), the temperature profiles are for $H(z)=1$.

Figure 1

Figure 2. Examples of non-uniform heating profiles in a non-dimensionalised domain with illustrative sketches of the conductive temperature profiles (black solid line) for fixed flux boundary conditions. In (a), the heating is localised near the upper boundary and in (b) near the lower boundary while being zero elsewhere, shown with red and white spaces, respectively. For (c) the heating is sinusoidal with a maximum at $z=0.25$ (red solid line) and a minimum of zero at $z=0.75$ (yellow solid line).

Figure 2

Figure 3. (a) Contour plot of $R_0$ as given in (4.1) with the inset (b) highlighting a region ($[0.925,1]\times [0.95,1]$) where $\lVert \eta \rVert _1 \sim \lVert \eta \rVert _2$. In (a) the green cross highlights uniform heating, drawn in (c), the blue cross highlights heating near the lower boundary drawn in (d), the yellow cross highlights heating near the upper boundary (e) and the black cross ($\times$) highlights sinusoidal heating, ( f).

Figure 3

Figure 4. Panel (a) plots heating profiles $H(z)$, with mean one, where the heating is uniform in a region $(0,\epsilon )$ near the lower boundary and zero elsewhere. In (a) eight cases are plotted of $\epsilon \in [0.05,0.5]$, where $\epsilon = 0.05$ is in yellow (yellow solid line) and $\epsilon =0.5$ in black (black solid line). Panel (b) plots $\epsilon$ against $R_0$, the value below which downwards conduction is ruled out. The vertical dashed line (- - -) corresponds to $\epsilon = 1.366 \times 10^{-7}$ intersecting the red line at $R_0=10^{22}$. For a given Rayleigh number (i.e. $10^{22}$) (b) can be used to find the value of $\epsilon$ for heating profiles in (a) below which downwards conduction is impossible.