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COUPLING OF WALL CONDUCTION WITH NATURAL CONVECTION FROM HEATED CYLINDERS IN A RECTANGULAR ENCLOSURE

机译:矩形壳体中壁对流与自然对流的耦合

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A numerical study has been conducted for natural convection heat transfer for air from two vertically separated horizontal heated cylinders confined to a rectangular enclosure having vertical walls of finite conductances and horizontal walls at the heat sink temperature. The interaction between convection in the fluid filled cavity and conduction in the vertical walls is investigated, Results have been obtained for Rayleigh numbers, Ra, between 10(3) and 10(6), dimensionless wall-fluid thermal conductivity ratio <(alpha)over bar> between 0.2 and 1000.0 and dimensionless wall thickness (W) over bar between 0.25 and 1.375. Results indicate that the Nusselt number along the vertical wall-fluid interface is a complex function of both Ra and <(alpha)over bar>. In general, the relative heat removal contribution by conduction in the wall through the top horizontal surface eta(N) decreases with Ra while that for the bottom surface eta(S) increases. For 0.2 less than or equal to <(alpha)over bar> less than or equal to 5.0, eta(S) is nearly independent of Ra. Moreover, for Ra greater than or equal to 10(5), 0.2 < <(alpha)over bar> less than or equal to 5.0 and 0.25 less than or equal to (W) over bar less than or equal to 1.375, eta(S), is independent of <(alpha)over bar> while eta(N) Lends to zero with increasing <(alpha)over bar>. [References: 7]
机译:已经进行了对空气的自然对流传热的数值研究,该空气来自两个垂直分离的水平加热缸,这些加热缸被限制在一个矩形外壳内,该外壳具有有限电导的垂直壁和在散热器温度下的水平壁。研究了充满流体的空腔中的对流与垂直壁中的传导之间的相互作用,获得了瑞利数Ra(介于10(3)和10(6)之间),无量纲的壁-流体导热系数<α的结果大于0.2到1000.0之间,无量纲的壁厚(W)在0.25到1.375之间。结果表明,沿垂直壁-流体界面的努塞尔数是Ra和<αoverbar>的复函数。通常,壁上通过顶部水平表面eta(N)的传导所产生的相对排热贡献随Ra的减小而减小,而用于底部表面eta(S)的相对排热贡献则随着增大。对于小于或等于0.2的小于或等于5.0,η(S)几乎与Ra无关。此外,对于Ra大于或等于10(5),在小于或等于1.375的Ra上,0.2 <<α超过或等于5.0,并且在0.25(W)下小于或等于0.25,小于等于(W)。 S)独立于<αoverbar>,而eta(N)随着<αoverbar>的增加而归零。 [参考:7]

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