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首页> 外文期刊>Physics of fluids >Direct numerical simulation of Rayleigh-Bénard convection in a cylindrical container of aspect ratio 1 for moderate Prandtl number fluid
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Direct numerical simulation of Rayleigh-Bénard convection in a cylindrical container of aspect ratio 1 for moderate Prandtl number fluid

机译:高普朗特数为1的纵横比为1的圆柱形容器中Rayleigh-Bénard对流的直接数值模拟

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A series of three-dimensional numerical simulations were conducted for the Rayleigh-Bénard convection in a cylindrical container with the aspect ratio γ = 1. The Prandtl number of the fluid is 7 and the Rayleigh number varies from 10 ~3 to 10 ~5. Results show that the aspect ratio of the cylinder has an important influence on the multiplicity of the steady flow state. The sidewall of the cylinder at γ = 1 restricts the increase of the number of rolls in the fluid layer. Therefore, only two-roll and single-roll flow patterns are observed at the whole simulation range of the Rayleigh number. During the transition of the Rayleigh-Bénard convection to the unsteady flow, it is found that the unsteady flow pattern and the bifurcation sequence of the oscillation flow are very sensitive to the initial condition.
机译:对于纵横比为γ= 1的圆柱形容器中的Rayleigh-Bénard对流进行了一系列三维数值模拟。流体的Prandtl数为7,Rayleigh数在10〜3到10〜5之间变化。结果表明,圆柱的长径比对稳态流动状态的多样性有重要影响。 γ= 1处的圆柱体侧壁限制了流体层中辊数的增加。因此,在瑞利数的整个模拟范围内只能观察到两辊和单辊的流型。在瑞利-贝纳德对流向非恒定流过渡的过程中,发现非恒定流模式和振荡流的分叉序列对初始条件非常敏感。

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