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NATURAL CONVECTION HEAT TRANSFER FROM VERTICAL 7x7 ROD BUNDLES IN LIQUID SODIUM

机译:液态钠中7x7垂直杆束的自然对流传热

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Natural convection heat transfer from vertical 7x7 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 PHOENICS code was used for the calculation considering the temperature dependence of thermo-physical properties concerned. The 7x7 test rods for diameter (D=7.6 mm), heated length (L=200 mm) and L/d (=26.32) were used in this work. The surface heat fluxes for each cylinder were equally given for a modified Rayleigh number, (R_(f,L))_ye and (R_(f,L))_(N_x.xNy,S/D), ranging from 3.08x10~4 to 4.28x10~7 (q=1x10~4~7x10~6 W/m~2) in liquid temperature (T_L=673.15 K). The values of S/D, which are ratios of the diameter of flow channel for bundle geometry to the rod diameter, for vertical 7x7 rod bundle were ranged from 1.8 to 6 on the bundle geometry with equilateral square array. 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))N_(xxNy,S/D), were clarified. The average value of Nusselt number, (Nu_(av))_(ij) and (Nu_(av,B))N_(xxNy,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, (R_(f,L))_(ij) and (R_(f,L))N_(xxNy,S/D) on heat transfer. The bundle geometry for the higher (Nu_(av,B)_(NxxNy,S/D) value under the condition of S/D=constant was examined. The general correlations for natural convection heat transfer from a vertical N_xxN_y rod bundle with the equilateral square and triangle arrays including the effects of array size, (R_(f,L))_(NxxNy,S/D) and S/D were derived. The correlations for vertical N_xxN_y rod bundles can describe the theoretical values of (Nu_(av,B))_(NxxNy,S/D) for each bundle geometry in the wide analytical range of S/D (=1.8 to 6) and the modified Rayleigh number ((R_(f,L))_(NxxNy,S/D)3.08x10~4 to 4.28xl07) within -9.49 to 10.6 % differences.
机译:对垂直7x7棒束在液态钠中的自然对流传热进行了数值分析,以优化具有等边正方形阵列ESA的束几何形状的热工液压设计。数值求解了由阶跃热通量引起的自然对流换热的非定常层流三维基本方程,直到溶液达到稳态。考虑到有关热物理性质的温度依赖性,使用了PHOENICS代码进行计算。在这项工作中使用了直径为(D = 7.6 mm),加热长度(L = 200 mm)和L / d(= 26.32)的7x7测试棒。对于修改后的瑞利数(R_(f,L))_ ye和(R_(f,L))_(N_x.xNy,S / D),均等地给出了每个圆柱体的表面热通量,范围为3.08x10〜液体温度(T_L = 673.15 K)为4至4.28x10〜7(q = 1x10〜4〜7x10〜6 W / m〜2)。对于垂直7x7棒束,S / D值(对于束几何形状的流道直径与杆直径之比)在具有等边正方形阵列的束几何形状上的范围为1.8到6。杆束的垂直单个圆柱的平均Nusselt数的空间分布(Nu_(av))_(ij)和垂直杆束的平均Nusselt数的空间分布(Nu_(av,B))N_(xxNy, S / D)。计算具有不同S / D值的束几何形状的Nusselt数(Nu_(av))_(ij)和(Nu_(av,B))N_(xxNy,S / D)的平均值,以检查阵列尺寸,束几何形状,S / D,(R_(f,L))_(ij)和(R_(f,L))N_(xxNy,S / D)对传热的影响。研究了在S / D =恒定的条件下较高(Nu_(av,B)_(NxxNy,S / D)值的束几何形状。推导了包括阵列尺寸,(R_(f,L))_(NxxNy,S / D)和S / D的等边正方形和三角形阵列。垂直N_xxN_y棒束的相关性可以描述(Nu (av,B))_(NxxNy,S / D)在S / D(= 1.8到6)的宽分析范围和修改后的瑞利数((R_(f,L))_(NxxNy ,S / D)差异在-9.49至10.6%之间,为3.08x10〜4至4.28x107)。

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