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NATURAL CONVECTIVE HEAT TRANSFER FROM A NARROW ISOTHERMAL VERTICAL FLAT PLATE WITH A UNIFORM HEAT FLUX AT THE SURFACE

机译:从狭窄的等温垂直平板上传热,在表面上具有均匀的热通量的窄等温垂直平板

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Natural convective flow over a vertical plate with a uniform heat flux over its surface has been numerically studied. When the plate is wide compared to its height the flow can be adequately modeled by assuming two-dimensional flow. However, when the width of the plate is relatively small compared to its height, the heat transfer coefficient can be considerably greater than that predicted by these two-dimensional flow results. The Nusselt number distribution over a narrow vertical plate, with a uniform heat flux at the plate surface, has been numerically determined. This heated plate is embedded in a plane adiabatic surface, the surface of the adiabatic surface being in the same plane as the heated plate. It has been assumed that the fluid properties are constant except for the density change with temperature which gives rise to the buoyancy forces, this having been treated by using the Boussinesq approach. It has also been assumed that the flow is symmetrical about the vertical centre-plane of the plate. The solution has been obtained by numerically solving the full three-dimensional form of the governing equations, these equations being written in dimensionless form. The solution has the Rayleigh number, the dimensionless plate width and the Prandtl number as parameters. Results have been numerically determined for a relatively wide range of Rayleigh numbers and dimensionless plate widths for a Prandtl number of 0.7. The dimensionless plate width has been found to have a significant influence on the mean Nusselt number for the plate when the plate is narrow and the Rayleigh number is low. The conditions under which three dimensional flow effects can be neglected have been deduced and an empirical equation for the mean Nusselt number for narrow plates with a uniform surface heat flux has been derived from the numerical results.
机译:在数值上研究了在其表面上具有均匀热通量的垂直板上的自然对流流。当板相比,与其高度相比,通过假设二维流动,可以充分建模流动。然而,当与其高度相比,当板的宽度相对较小时,传热系数可以远大于通过这些二维流动结果预测的热量系数。在单板表面上具有均匀的热通量的窄垂直板上的露天数分布已经在数值上确定。该加热板嵌入平面绝热表面中,绝热表面的表面与加热板相同的平面。已经假设除了具有浮力力的温度的密度变化之外,流体性质是恒定的,这使得通过使用Boussinesq方法处理。还假设流动围绕板的垂直中心平面对称。通过数值求解控制方程的全三维形式来获得解决方案,这些方程以无量纲形式写成。该解决方案具有瑞利数,无量纲板宽度和Prandtl编号作为参数。结果已经在数值上确定了相对宽的瑞利数和无量纲板宽度,用于0.7的Prandtl数。已经发现无量纲板宽度对板的平均良好数量有显着影响,当板窄时,瑞利数低。已经推导出忽略三维流动效应的条件,并且已经衍生出具有均匀表面热通量的窄板的平均良好数量的经验方程已经来自数值结果。

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