Heat transport by turbulent Rayleigh–Bénard convection for Pr ≃ 0.8 and 3 × 1012 ≲ Ra ≲ 1015: aspect ratio Γ = 0.50
نویسندگان
چکیده
We report on the experimental results for heat-transport measurements, in the form of the Nusselt number Nu, by turbulent Rayleigh–Bénard convection (RBC) in a cylindrical sample of aspect ratio 0 ≡ D/L = 0.50 (D = 1.12m is the diameter and L = 2.24m the height). The measurements were made using sulfur hexafluoride at pressures up to 19 bar as the fluid. They are for the Rayleigh-number range 3× 1012 . Ra . 1015 and for Prandtl numbers Pr between 0.79 and 0.86. For Ra < Ra 1 ' 1.4× 10 13 we find Nu = N0 Raeff with γeff = 0.312± 0.002, which is consistent with classical turbulent RBC in a system with laminar boundary layers below the top and above the bottom 7 Author to whom any correspondence should be addressed. Content from this work may be used under the terms of the Creative Commons Attribution-NonCommercialShareAlike 3.0 licence. Any further distribution of this work must maintain attribution to the author(s) and the title of the work, journal citation and DOI. New Journal of Physics 14 (2012) 103012 1367-2630/12/103012+39$33.00 © IOP Publishing Ltd and Deutsche Physikalische Gesellschaft
منابع مشابه
Heat transport by turbulent Rayleigh–Bénard convection for Pr ≃ 0.8 and 4 × 1011 ≲ Ra ≲ 2 × 1014: ultimate-state transition for aspect ratio Γ = 1.00
We report experimental results for heat-transport measurements, in the form of the Nusselt number Nu, by turbulent Rayleigh–Bénard convection (RBC) in a cylindrical sample of aspect ratio 0 ≡ D/L = 1.00 (D = 1.12m is the diameter and L = 1.12m the height) and compare them with previously reported results for 0 = 0.50. The measurements were made using sulfur hexafluoride at pressures up to 19 ba...
متن کاملHeat transport in turbulent Rayleigh - Bénard convection for Pr ≃ 0 . 8 and Ra ≲ 1015
We report experimental results for the heat transport, as expressed by the Nusselt number Nu, by turbulent Rayleigh-Bénard convection in a cylindrical sample of aspect ratio Γ ≡ D/L = 0.50 (D = 1.12 m is the diameter and L = 2.24 m the height). The measurements are for the Rayleigh-number range 10 <∼ Ra <∼ 10 15 and for a Prandtl number Pr ' 0.86. At these large Ra the results were exceptionall...
متن کاملLogarithmic temperature profiles in the bulk of turbulent Rayleigh–Bénard convection for a Prandtl number of 12.3
We report measurements of logarithmic temperature profiles Θ(z, r)=A(r)× ln(z/L)+ B(r) in the bulk of turbulent Rayleigh–Bénard convection (here Θ is a scaled and timeaveraged local temperature in the fluid, z is the vertical and r the radial position, and L is the sample height). Two samples had aspect ratios Γ ≡D/L= 1.00 and 0.50 (where D = 190 mm is the diameter). The fluid was a fluorocarbo...
متن کاملTurbulent Rayleigh–Bénard convection in a cylindrical container with aspect ratio Γ = 0.50 and Prandtl number P r = 4.38
Measurements of the Nusselt number and properties of the large-scale circulation (LSC) are presented for turbulent Rayleigh–Bénard convection in water-filled cylindrical containers (Prandtl number Pr =4.38) with aspect ratio Γ =0.50. They cover the range 2× 10 <∼ Ra <∼ 1× 10 of the Rayleigh number Ra. We confirm the occurrence of a double-roll state (DRS) of the LSC and focus on the statistics ...
متن کاملHeat transport by turbulent rotating Rayleigh–Bénard convection and its dependence on the aspect ratio
We report on the influence of rotation about a vertical axis on heat transport by turbulent Rayleigh–Bénard convection in a cylindrical vessel with an aspect ratio Γ ≡ D/L = 0.50 (D is the diameter and L the height of the sample) and compare the results with those for larger Γ . The working fluid was water at Tm = 40 ◦C where the Prandtl number Pr is 4.38. For rotation rates Ω . 1 rad s−1, corr...
متن کاملذخیره در منابع من
با ذخیره ی این منبع در منابع من، دسترسی به آن را برای استفاده های بعدی آسان تر کنید
عنوان ژورنال:
دوره شماره
صفحات -
تاریخ انتشار 2012