棒束通道流动阻力与传热特性实验研究

Zhiqiang Zhu, Chunping Tian, Chang-qi Yan, Jianjun Wang, Tingting Ren, Zehua Guo
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引用次数: 1

摘要

采用单相自然循环实验,研究了在杆距与杆外径比(P/D)为1.38的3 × 3棒束通道内的流动阻力和换热特性。进气过冷度范围为30 ~ 90K,加热功率为1 ~ 20kW。棒是用恒定的热流加热的。根据实验结果划分了自然循环条件下的流型,认为转捩雷诺数为800。由于杆束通道内的流动过渡不如圆管内明显,因此可以通过摩擦系数曲线的斜率变化来识别流动过渡。同时,与圆管和矩形通道等规则通道相比,棒束内的流动转变要早得多,上临界雷诺数也要大得多。拟合了层流态和跃迁态的两个关系式来计算摩擦系数。对于栅格隔板局部阻力系数,在雷诺数为800时变化不大,同样拟合两种相关性来计算局部阻力系数。努塞尔数趋势在4000雷诺数附近发生变化,但在过渡点保持不变,说明流动转变对换热没有明显影响。对不同的单相对流换热关系式的换热结果进行了比较。D-B关系式和Gnielinski关系式不适用于杆束通道的换热预测,相对偏差大于20%。在高雷诺数区域,Weisman、Presser和Markoczy相关预测效果较好,其中Markoczy相关预测效果最好。在低雷诺数区域,大多数实验结果大于相关系数。基于D-B关联的方法可能不适合杆束通道的传热预测,需要提出一种新的关联方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Experimental Research on the Flow Resistance and Heat Transfer Characteristics in Rod Bundle Channel
Single-phase natural circulation experiments were conducted to study the flow resistance and heat transfer characteristics in a 3 × 3 rod bundle channel with the ratio of rod pitch and rod outer diameter (P/D) 1.38. The range of inlet subcooling degree is 30∼90K and the heating power is 1∼20kW. The rods are heated with constant heat flux. According to the experimental results, the flow regime under natural circulation condition is divided and the transition Reynolds number is considered as 800. The flow transition is recognized by the slope change of friction factor curve since the flow transition in the rod bundle channel is not as obvious as that in round pipe. Simultaneously, the flow transition in the rod bundle is much earlier and the upper critical Reynolds number is much larger compared to regular channel like round pipe and rectangular channel. Two correlations for laminar and transition regime are fitted to calculate the friction factor. As for the grid spacer local resistance coefficient, there is slight change at Reynolds number 800 and similarly two correlations are fitted to calculate the local resistance coefficient. The Nusselt number tendency changes at around Reynolds number 4000 but keep unchanged at transition point, which means the flow transition has no obvious effect to the heat transfer. The heat transfer results are compared with different single-phase convective heat transfer correlations. D-B and Gnielinski correlations are not suitable for the heat transfer prediction in rod bundle channel and the relative deviation is more than 20%. Weisman, Presser and Markoczy correlations predict relatively well in high Reynolds number region, and Markoczy correlation is the best of them. In low Reynolds number region, most experimental results are larger than the correlations. D-B correlation based methods may be unsuitable for the heat transfer prediction in rod bundle channel and a new correlation needs to be proposed.
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