2018
DOI: 10.1017/jfm.2018.507
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Bulk temperature and heat transport in turbulent Rayleigh–Bénard convection of fluids with temperature-dependent properties

Abstract: We critically analyse the different ways to evaluate the dependence of the Nusselt number ($\mathit{Nu}$) on the Rayleigh number ($\mathit{Ra}$) in measurements of the heat transport in turbulent Rayleigh–Bénard convection under general non-Oberbeck–Boussinesq conditions and show the sensitivity of this dependence to the choice of the reference temperature at which the fluid properties are evaluated. For the case when the fluid properties depend significantly on the temperature and any pressure dependence is i… Show more

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Cited by 31 publications
(28 citation statements)
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References 49 publications
(78 reference statements)
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“…The experiments used pressurized sulfur hexafluoride (SF 6 ) and were performed over a large parameter space in the High Pressure Convection Facility (HPCF, 2.24 m high) at the Max Planck Institute for Dynamics and Self-Organization in Göttingen [30]. In the studied parameter range, the Oberbeck-Boussinesq approximation is valid [31][32][33], and the centrifugal force is negligible [8,34,35].…”
mentioning
confidence: 99%
“…The experiments used pressurized sulfur hexafluoride (SF 6 ) and were performed over a large parameter space in the High Pressure Convection Facility (HPCF, 2.24 m high) at the Max Planck Institute for Dynamics and Self-Organization in Göttingen [30]. In the studied parameter range, the Oberbeck-Boussinesq approximation is valid [31][32][33], and the centrifugal force is negligible [8,34,35].…”
mentioning
confidence: 99%
“…There is a considerable analytical and numerical effort to solve Boussinesq approximations or similar forms both for waves [29][30][31][32][33][34][35][36][37][38] and for dissipative dynamics with possible density variations [39][40][41][42][43]. Experiments for certain parameter values are also realized [44][45][46].…”
Section: Introductionmentioning
confidence: 99%
“…In general, the variations of fluid parameters between the warm bottom and the cold top destroy the up-down symmetry of the system, resulting in T c = T m , with T m being the average temperature T m = (T t + T b )/2. For liquids, T c > T m was observed [11][12][13][14][15][16][17], while T c < T m was found for gases as the working fluid [14,[18][19][20][21]. Various models predicting T c as a function of , T m , and fluid parameters have been proposed and predict T c more or less accurately.…”
Section: Introductionmentioning
confidence: 99%
“…Ahlers et al [14,19] assumed laminar boundary layers at the bottom and top and solved numerically the momentum and heat equation assuming temperature-dependent fluid properties, while neglecting buoyancy. There is also the virtual cell model [20] that predicts T c by assuming that the top part and the bottom part of the convection system can be described as two separate OB systems that both follow the same Nu(Ra) relation.…”
Section: Introductionmentioning
confidence: 99%
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