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Natural convection heat transfer from a horizontal cylinder in liquid sodium Part 1: Experimental results

机译:液钠中水平圆柱体的自然对流传热第1部分:实验结果

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Natural convection heat transfer from horizontal 7.6 and 10.7 mm diameter test cylinders to liquid sodium were measured for the heat fluxes ranging from 8 × 10~3 to 2.64 × 10~6 W/m~2. The average Nusselt numbers for 7.6- and 10.7 mm diameter test cylinders are in good agreement with each other in the overlapping range of 1.5 ≤ GrPr~2/(1 + Pr) ≤ 35 on the graph of log Nu versus log GrPr~2/(1 + Pr). The average Nusselt numbers were obtained for GrPr~2/(1 + Pr) from 0.2 to 120 (41 ≤ Ra ≤ 25 650) as a single curve on the graph by using these two different diameter cylinders. The average Nusselt numbers become higher than the values predicted by the correlation of Kutateladze et al. from 36 to 100 with decreasing Rayleigh numbers. It was assumed that this is because the boundary layer approximation by which the correlation was derived becomes inappropriate as the thermal boundary layer becomes thicker compared with the cylinder diameter with decreasing Rayleigh numbers. The natural convection heat transfer correlation of Churchill and Chu, that of Hyman et al. and that of Sugiyama et al. underpredicted the experimental results about 20, from 43 to 66, and from 8 to 14, respectively.
机译:测量了从水平7.6和10.7 mm直径的测试筒到液态钠的自然对流传热,其热通量为8×10〜3至2.64×10〜6 W / m〜2。在对数Nu相对于对数GrPr〜2 /的曲线图上1.5≤GrPr〜2 /(1 + Pr)≤35的重叠范围内,直径为7.6和10.7 mm的测试圆柱体的平均Nusselt数彼此之间具有很好的一致性。 (1 + Pr)。使用这两个不同直径的圆柱体,GrPr〜2 /(1 + Pr)的平均Nusselt数从0.2到120(41≤Ra≤25 650)从图中获得为一条曲线。平均Nusselt数变得高于Kutateladze等人的相关性预测的值。瑞利数从36减少到100。可以认为这是因为,随着瑞利数减少,与圆筒直径相比,热边界层变厚,由此推导相关的边界层近似变得不合适。丘吉尔和楚的自然对流传热相关性,海曼等人。和杉山等人的分别低估了约20个实验结果(从43到66,以及从​​8到14)。

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