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Experimental Characterization of Pressure Drops and Channel Instabilities in Helical Coil SG Tubes

机译:螺旋线圈SG管中的压降和通道不稳定性的实验表征

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Helical tube heat exchangers provide better heat transfer characteristics, an improved capability to accommodate stresses due to thermal expansions and a more compact design with respect to straight tube heat exchangers. For these advantages they are considered as an option for the Steam Generator (SG) of many new reactor projects of Generation Ⅲ+ and Generation IV. In particular, their compactness fits well with the requirements of Small-medium Modular Reactors (SMRs) of integral design, where all the primary system components are located inside the reactor vessel. In this framework, thermal hydraulics of helical pipes has been studied in recent years by Politecnico di Milano in different experimental campaigns. Experiments have been carried out in a full-scale open loop test facility installed at SIET labs in Piacenza, Italy, to simulate the SG of a typical SMR. The facility includes two helical pipes (1 m coil diameter, 32 m length, 8 m height), connected via lower and upper headers. Following recently completed experimental campaigns dedicated to pressure drops and density wave instabilities, this paper deals with a new experimental campaign focused on both pressure drops (single-phase flow and two-phase flow, laminar and turbulent regimes) and flow instabilities. The availability of a large number of experimental data, in particular on two-phase flow, is of fundamental interest for correlation development, model validation and code assessment. Two-phase pressure drops have been measured in adiabatic conditions, ranging from 200 to 600 kg/m~2s for the mass flux, from 30 to 60 bar for the pressure and from 0.1 to 1.0 for the flow quality. The channel characteristics mass flow rate -pressure drop has been determined experimentally in the range 10 - 40 bar, varying the mass flow rate at a fixed value of the thermal flux. In addition, single-phase pressure drops have been measured in both laminar and turbulent conditions. Density wave instabilities have been studied at mass flux from 100 to 400 kg/m~2s and pressure from 10 to 20 bar , to confirm the particular behavior of the stability boundary in helical geometry at low pressure and low mass flow rate. Finally, starting from the unstable regions identified from the experimental channel characteristics, Ledinegg type instabilities have been investigated to drawn stability maps with complete stable and unstable regions in the dimension less plane N_(sub)-N_(pch).
机译:螺旋管式换热器具有更好的传热特性,具有更好的承受因热膨胀引起的应力的能力,并且相对于直管式换热器而言,设计更为紧凑。由于这些优点,它们被认为是Ⅲ+和IV代许多新反应堆项目的蒸汽发生器(SG)的选装件。特别是,它们的紧凑性非常适合整体设计的中小型模块化反应堆(SMR)的要求,其中所有主要系统组件均位于反应堆容器内部。在这种框架下,近年来米兰理工大学在不同的实验活动中研究了螺旋管的热工水力。实验已在意大利皮亚琴察SIET实验室安装的大型开环测试设备中进行,以模拟典型SMR的SG。该设施包括两个螺旋管(盘管直径1 m,长度32 m,高度8 m),通过上下集管连接。在最近完成了专门针对压降和密度波不稳定性的实验活动之后,本文针对以压降(单相流和两相流,层流和湍流状态)和流不稳定性为重点的新实验活动进行了研究。大量实验数据的可用性,尤其是两相流的数据,对于相关性开发,模型验证和代码评估至关重要。在绝热条件下测量了两相压降,质量通量为200至600 kg / m〜2s,压力为30至60 bar,流动质量为0.1至1.0。已经通过实验确定了通道特性的质量流量-压降在10-40 bar的范围内,以固定的热通量值改变了质量流量。另外,已经在层流和湍流条件下测量了单相压降。研究了在质量通量为100至400 kg / m〜2s和压力为10至20 bar的情况下的密度波不稳定性,以确认在低压和低质量流量下螺旋几何形状中稳定边界的特殊行为。最后,从实验通道特征确定的不稳定区域开始,研究了Ledinegg型不稳定性,以绘制出维数较少的平面N_(sub)-N_(pch)中具有完全稳定和不稳定区域的稳定性图。

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