Abstract

In Rayleigh–Bénard convection experiments, the thermal coupling between the sidewall and fluid is unavoidable. As a result, the thermal properties of the sidewall can influence the flow structure that develops. To get a better understanding of the influence of the sidewall, we performed a one-to-one comparison between experiments and direct numerical simulations (DNS) in aspect ratio (diameter over height) $\unicode[STIX]{x1D6E4}=1.00$ samples. We focus on the global heat transport, i.e. the Nusselt number $Nu$, and the local vertical temperature gradients near the horizontal mid-plane on the cylinder axis and close to the sidewall. The data cover the range $10^{5}\lesssim Ra\lesssim 10^{10}$ where $Ra$ is the Rayleigh number. The $Nu$ number obtained from experimental measurements and DNS, in which we use an adiabatic sidewall, agree well. The experiments are performed with several gases, which have widely varying thermal conductivities, but all have a Prandtl number $Pr\approx 0.7$. For $Ra\gtrsim 10^{7}$, both experiments and DNS reveal a stabilizing (positive) temperature gradient at the cylinder axis. This phenomenon was known for high $Pr$, but had not been observed for small $Pr\approx 0.7$ before. The experiments reveal that the temperature gradient decreases with decreasing $Ra$ and eventually becomes destabilizing (negative). The decrease appears at a higher $Ra$ when the sidewall admittance, which measures how easily the heat transfers from the fluid to the wall, is smaller. However, the simulations with an adiabatic sidewall do not reproduce the destabilizing temperature gradient at the cylinder axis in the low $Ra$ number regime. Instead, these simulations show that the temperature gradient increases with decreasing $Ra$. We find that the simulations can reproduce the experimental findings on the temperature gradient at the cylinder axis qualitatively when we consider the physical properties of the sidewall and the thermal shields. However, the temperature gradients obtained from experiments and simulations do not agree quantitatively. The reason is that it is incredibly complicated to reproduce all experimental details accurately due to which it is impossible to reproduce all experimental measurement details. The simulations show, in agreement with the models of Ahlers (Phys. Rev. E, vol. 63 (1), 2000, 015303) and Roche et al. (Eur. Phys. J. B, vol. 24 (3), 2001, pp. 405–408), that the sidewall can act as an extra heat conductor, which absorbs heat from the fluid near the bottom plate and releases it into the fluid near the top plate. The importance of this effect decreases with increasing $Ra$. A crucial finding of the simulations is that the thermal coupling between the sidewall and fluid can strongly influence the flow structure, which can result in significant changes in heat transport. Since this effect goes beyond a simple short circuit of the heat transfer through the sidewall, it is impossible to correct experimental measurements for this effect. Therefore, careful design of experimental set-ups is required to minimize the thermal interaction between the fluid and sidewall.

Highlights

  • Rayleigh–Bénard convection, i.e. the convection of a horizontal fluid layer heated from below and cooled from above, is an excellent model system to study heat transfer and thermally induced turbulence

  • We focus on the global heat transport, i.e. the Nusselt number Nu, and the local vertical temperature gradients near the horizontal mid-plane on the cylinder axis and close to the sidewall

  • While these data agree with the direct numerical simulations (DNS) for Ra 1010, they are larger than the simulation results for lower Ra, with the difference reaching 16 % below Ra 109

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Summary

Introduction

Rayleigh–Bénard convection, i.e. the convection of a horizontal fluid layer heated from below and cooled from above, is an excellent model system to study heat transfer and thermally induced turbulence. The reason is that the vertical temperature profile in the sidewall differs from that in the convecting fluid and there is a lateral heat exchange between sidewall and fluid, which can influence the flow dynamics To further explore these issues, Verzicco (2002) performed DNS of Rayleigh–Bénard convection in a cylindrical container with. We use the simulations to test various sidewall configurations to assess the influence of different sample designs To achieve this we employ, in contrast to most DNS, a more realistic model based on the Navier–Stokes–Brinkman equation in combination with the immersed boundary method to simulate the effect of the sidewall and insulation layers as a conjugate heat transfer problem.

The apparatus
Numerical procedures
Results for the Nu number
Effect of the sidewall
Summary and conclusions
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