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A new buoyancy model replacing the standard pseudo-density difference for internal natural convection in gases

机译:一种新的浮力模型,代替了气体内部自然对流的标准伪密度差

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Natural convection in enclosed spaces has been analyzed and numerically evaluated using a direct buoyancy model which replaces the pseudo-density difference which has been heretofore standard in all previous studies of internal natural convection of gases. It was demonstrated conclusively that the pseudo-density-difference model is totally irrelevant to the physical processes which create the buoyancy. When properly accounted, the presence of the pseudo-density difference does no harm, but it provides a source of confusion for the source of the buoyant forces which create motion. This conclusion was drawn from numerical solutions of three-dimensional natural convection in an oven-like cavity. These solutions were irrefutably supported by experimental data. It was also demonstrated that accounting for the naturally occurring pressure variations within the enclosed space had a negligible effect upon the surface heat transfer coefficients. The commonly used Boussinesq equation of state was found to provide accurate surface heat transfer results provided that the density, thermal conductivity, viscosity, and coefficient of thermal expansion are evaluated at a temperature that is the average of the temperatures of the surfaces which bound the enclosed space.
机译:已使用直接浮力模型对封闭空间中的自然对流进行了分析和数值评估,该模型取代了以前在所有内部气体自然对流研究中均已采用的伪密度差。结论性地表明,伪密度差模型与产生浮力的物理过程完全无关。如果适当地考虑,伪密度差的存在没有害处,但是它为产生运动的浮力源提供了混乱的根源。该结论是根据烤箱状腔中三维自然对流的数值解得出的。这些解决方案得到实验数据的无可辩驳的支持。还证明了解决封闭空间内自然发生的压力变化对表面传热系数的影响可忽略不计。发现常用的Boussinesq状态方程式可提供准确的表面传热结果,条件是在密度为一定值的温度下对密度,导热率,粘度和热膨胀系数进行评估,该温度是限定封闭区域的表面温度的平均值空间。

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