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Influence of geometrical parameters on convective flows in non-uniformly heated cylindrical fluid layers

机译:几何参数对非均匀加热圆柱形流体层中的对流流的影响

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Convection in a fluid layer with a free surface in a cylindrical container non-homogeneously heated from below was studied experimentally. The heater has a circular form and was placed in the center of the vessel. Such a system in the presents of rotation is very promising for studying the nature of tropical cyclones. In current paper we considered the influence of different geometric parameters on the dynamics of convection flows. For it two experimental setups of different sizes were used. Measurements were done for fluids with different values of Prandtl number and heating powers. It was shown that the structure and intensity of mean flow producing by a horizontal temperature gradient are defined by Rayleigh number Ra. The basic flow leads to unstable temperature stratification over the heating area and the formation of a system of secondary flows. The formation of secondary flows depends on characteristics of thermal boundary layer and is described by local Rayleigh number Ra_δ.
机译:实验研究了在下面从下面的圆柱形容器中的具有自由表面的流体层中的对流。加热器具有圆形形式,并放置在容器的中心。在旋转礼物的情况下,这种系统非常有希望用于研究热带气旋的性质。在目前的论文中,我们考虑了不同几何参数对对流流动动态的影响。对于它使用了两个不同尺寸的实验设置。为具有Prandtl数量和加热功率的不同值的流体进行测量。结果表明,通过水平温度梯度产生的平均流量的结构和强度由瑞利数Ra限定。基本流动在加热面积上导致不稳定的温度分层和二次流动系统的形成。二次流动的形成取决于热边界层的特性,并通过本地瑞利码Ra_Δ描述。

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