核电厂滞止支管湍流渗透长度评估准则的对比分析与试验研究
ANALYSIS AND EXPERIMENTAL COMPARATIVE STUDY ON TURBULENT PENETRATION LENGTH ASSESSMENT CRITERIA FOR STAGNANT BRANCH PIPES IN NUCLEAR POWER PLANTS
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摘要: 国际上多起管道裂纹事件表明, 核电厂关键系统相连的滞止支管内, 稳定运行下主管高温流体可能经湍流渗透侵入低温滞止流体, 形成动态迁移的冷热交界面并诱发热循环, 威胁管道结构完整性. 针对该类风险快速评估的需求和滞止结构高温试验数据缺乏的现状, 本文以下行水平(Down-Horizontal, DH)滞止支管为对象搭建高温试验装置, 开展湍流渗透及热循环试验, 并对日本机械工程师学会(Japan Society of Mechanical Engineers, JSME)准则与美国材料可靠性计划(Materials Reliability Program, MRP)准则进行了对比分析. 试验结果表明: 弯管及水平管段可观察到明显的冷热交界面, 以及对应典型热循环的管壁温度波动; 与60 °C工况相比, 180 °C(滞止端20 °C)工况的雷诺数增至2.8倍, 但主支管密度差增至7.3倍, 浮升力对湍流渗透的抑制超过湍流强度的增强, 渗透长度随主管温度升高反而减小. 对两准则的对比分析表明, JSME 准则仅适用于 DH 结构, 但适用流速范围宽, 小管径下预测结果偏保守; JSME准则仅适用于DH结构, 但适用流速范围宽, 小管径下预测偏保守; MRP准则涵盖结构更多、量化数据更全面, 但未充分考虑运动粘度随温度的变化. 基于同源试验数据还发现, 两准则预测的湍流渗透长度均涵盖实测最大值并有约2倍支管内径的裕度, 但相同工况下可能给出相反的风险评估结论. 工程应用中宜结合工况与管线尺寸取两者预测结果的包络作为联合判据, 以提高评估可靠性.Abstract: Pipe cracking events reported internationally have shown that, in stagnation branch pipes connected to key systems of nuclear power plants, high-temperature fluid from the main pipe can intrude into the low-temperature stagnant fluid during steady operation through turbulent penetration, forming a dynamically migrating hot-cold interface and inducing thermal cycling that threatens the structural integrity of the pipe. Addressing the need for rapid assessment of this type of risk and the current lack of high-temperature test data on stagnant structures, this paper builds a high-temperature test facility for down-horizontal (DH) stagnation branch pipes, conducts turbulent penetration and thermal cycling tests, and compares the Japan Society of Mechanical Engineers (JSME) guideline with the Materials Reliability Program (MRP) guideline. The test results show a clear hot-cold interface in the elbow and horizontal pipe sections, together with wall temperature fluctuations corresponding to typical thermal cycling. Relative to the 60 °C case, the 180 °C case (stagnation flange at 20 °C) raises the Reynolds number by a factor of 2.8 but the density difference between the main and branch pipes by a factor of 7.3; the buoyancy suppression of turbulent penetration then outweighs the enhancement of turbulence intensity, so the penetration length decreases rather than increases with rising main pipe temperature. The comparison shows that the JSME guideline applies only to DH configurations but covers a wide flow-velocity range and yields conservative predictions for small pipe diameters, whereas the MRP guideline covers more configurations and more extensive quantitative data but does not sufficiently account for the temperature dependence of kinematic viscosity. Using the same test data, it is further found that the penetration lengths predicted by both guidelines cover the measured maximum with a margin of about twice the branch pipe inner diameter, yet under identical cases the two guidelines may lead to opposite risk-assessment conclusions. In engineering practice, the envelope of the two predictions should be adopted as a combined criterion according to the operating case and pipe dimensions, so as to improve the reliability of the assessment.
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