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首页> 外文期刊>Journal of nuclear engineering and radiation science >Laminar Natural Convection Heat Transfer From Vertical 7?×?7 Rod Bundles in Liquid Sodium
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Laminar Natural Convection Heat Transfer From Vertical 7?×?7 Rod Bundles in Liquid Sodium

机译:层层自然对流热传递从垂直7?×7杆束液钠

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Laminar natural convection heat transfer from vertical 7?×?7?rod bundle in liquid sodium was numerically analyzed to optimize the thermal–hydraulic design for the bundle geometry with equilateral square array (ESA). The unsteady laminar three-dimensional basic equations for natural convection heat transfer caused by a step heat flux were numerically solved until the solution reaches a steady-state. The code of the parabolic hyperbolic or elliptic numerical integration code series (PHOENICS) was used for the calculation considering the temperature dependence of thermophysical properties concerned. The 7?×?7 heated rods for diameter (D?= ? 0.0076 m), length (L?= ? 0.2 m) and L/D (=26.32) were used in this work. The surface heat fluxes for each cylinder, which was uniformly heated along the length, were equally given for a modified Rayleigh number, (Ra _( f,L ) ) _( ij ) and (Ra _( f,L ) ) _( Nx×Ny,S/D ) , ranging from 3.08?×?10 ~( 4 ) to 4.28?×?10 ~( 7 ) (q?= ? 1?×?10 ~( 4 ) ~7?×?10 ~( 6 ) W/m ~( 2 ) ) in liquid temperature (T _( L ) ?=?673.15 K). The values of ratio of the diagonal center-line distance between rods for bundle geometry to the rod diameter (S/D) for vertical 7?×?7?rod bundle were ranged from 1.8 to 6 on the bundle geometry with ESA. The spatial distribution of average Nusselt numbers for a vertical single cylinder of a rod bundle, (Nu _( av ) ) _( ij ) , and average Nusselt numbers for a vertical rod bundle, (Nu _( av ) _( ,B ) ) _( Nx×Ny,S/D ) , were clarified. The average values of Nusselt number, (Nu _( av ) ) _( ij ) and (Nu _( av ) _( ,B ) ) _( Nx×Ny,S/D ) , for the bundle geometry with various values of S/D were calculated to examine the effect of array size, bundle geometry, S/D, (Ra _( f,L ) ) _( ij ) and (Ra _( f,L ) ) _( Nx×Ny,S/D ) on heat transfer. The bundle geometry for the higher (Nu _( av ) _( ,B ) ) _( Nx×Ny,S/D ) value under the condition of S/D?=?constant was examined. The general correlations for natural convection heat transfer from a vertical N _( x ) ×N _( y ) rod bundle with the ESA and equilateral triangle array (ETA), including the effects of array size, (Ra _( f,L ) ) _( Nx×Ny,S/D ) and S/D were derived. The correlations for vertical N _( x ) ×N _( y ) rod bundles can describe the theoretical values of (Nu _( av ) _( ,B ) ) _( Nx×Ny,S/D ) for each bundle geometry in the wide analytical range of S/D (=1.8–6) and the modified Rayleigh number ( (Ra _( f,L ) ) _( Nx×Ny,S/D ) ?=?3.08?×?10 ~( 4 ) to 4.28?×?10 ~( 7 ) ) within ?9.49 to 10.6% differences.
机译:从垂直7?×7×7?7中的层状自然对流热传递液体钠中的杆束,以优化具有等边方形阵列(ESA)的束几何形状的热液压设计。用阶梯热通量引起的自然对流传热的非定常流动三维基本方程在数值上进行了数值求解,直到溶液达到稳态。考虑到热物理性质的温度依赖性,使用抛物线双曲或椭圆数数值整合码系列(噬菌体)的代码进行计算。对于直径(D?= 0.0076米),7××7加热棒,在这项工作中使用长度(L?= 0.2米)和L / D(= 26.32)。沿长度均匀加热的每个圆柱体的表面热通量同等地给予修改的瑞利数(RA _(F,L))_(IJ)和(RA _(F,L))_( NX×NY,S / D),从3.08?×10〜(4)到4.28?×10〜(7)(q?=?1?×10〜(4)〜7?×10 〜(6)在液体温度下(t _(l)?=α673.15k)中的w / m〜(2))。对于垂直7Ω·×7Ω·7Ω·杆束的束几何形状与杆直径(S / D)的杆之间的对角线中心线距离的比例值在束几何形状的1.8至6中,与ESA。杆束的垂直单缸的平均衬柱的空间分布,(nu _(av))_(ij)和垂直杆束的平均衬布号(nu _(av)_(,b) )_(NX×NY,S / D)澄清。 NUSERET编号的平均值(nu _(av))_(ij)和(nu _(av)_(,b))_(nx×ny,s / d),对于具有各种值的捆绑几何计算S / D以检查阵列大小,束几何,S / D的效果,(RA _(F,L))_(IJ)和(RA _(F,L))_(nx×ny,s / d)在传热上。在S / D的条件下,较高的(NU _(AV)_(,b))_(nx×ny,s / d)值的束几何图形。自然对流热传递的一般相关性来自垂直N _(x)×n _(y)杆束与ESA和等边三角形阵列(ETA),包括阵列大小的效果,(RA _(F,L) )_(纳米×ny,s / d)和s / d。垂直N _(x)×n _(y)杆束的相关性可以描述每个束几何形状的(nu _(av)_(,b))_(nx×ny,s / d)的理论值S / D(= 1.8-6)和修改的瑞利数的宽分析范围((Ra_(f,l))_(nx×ny,s / d)?=?3.08?×10〜(4在4.28?×10〜(7)内)差异9.49至10.6%。

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