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Numerical analysis of natural convection in sodium plenum below the grid plate of a fast reactor during a severe accident

机译:严重事故中快堆栅板下方钠气室自然对流的数值分析

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Heat transfer characteristics of liquid sodium are quite different from that of normal liquids because of its very low Prandtl number. Empirical correlations for convective heat transfer in sodium are rather limited because of inherent difficulties in performing sodium experiments. In this paper, transient and steady natural convection developing inside a cylindrical enclosure heated from the top and cooled along the vertical side wall is studied by a numerical analysis. This problem is of relevance to the safety analysis of sodium cooled pool type fast reactor. The focus of the present investigation is to determine the effect of plate thickness on the natural convection heat transfer characteristics. For the case of a thick top plate, in the transient regime, heat transfer is conduction dominated and Nusselt number is found to be inversely proportional to square root of time as in the case of a thin plate. But the steady state heat transfer coefficient between the lower surface of thick hot plate and liquid sodium is less by about 25% than for a thin plate at the same temperature as the lower surface. The reason for this behaviour is traced to the weaker convective current developed in the case of a thick plate. Based on detailed parametric studies, a correlation for Nusselt number is derived with a correlation coefficient of 0.99, for use in the reactor safety analysis. The Nusselt number is found to be a function of Boussinesq number, thermal conductivity ratio between the wall material and liquid sodium and non-dimensional thickness of the plate. The validity of the correlation is further checked by applying it to different data sets not used for the derivation of the correlation.
机译:液态钠的传热特性因其极低的普朗特数而与普通液态的传热特性完全不同。钠中对流传热的经验相关性相当有限,因为在进行钠实验中存在固有的困难。在本文中,通过数值分析研究了从顶部加热并沿垂直侧壁冷却的圆柱形外壳内部瞬态和稳态自然对流。这个问题与钠冷池式快堆的安全性分析有关。本研究的重点是确定板厚对自然对流换热特性的影响。对于较厚的顶板,在瞬态状态下,热传导受传导支配,与薄板的情况一样,发现努塞尔数与时间的平方根成反比。但是,在与下表面相同的温度下,厚热板的下表面与液态钠之间的稳态传热系数比薄板的稳态传热系数小约25%。出现这种现象的原因可归因于厚板情况下产生的较弱对流。根据详细的参数研究,得出努塞尔数的相关性,相关系数为0.99,用于反应堆安全性分析。发现Nusselt数是Boussinesq数,壁材料和液体钠之间的导热系数以及板的无尺寸厚度的函数。通过将相关性应用于未用于相关性推导的不同数据集,可以进一步检查相关性的有效性。

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