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    不同工况下核能换热系统及蒸发器的模拟研究

    Simulation study of nuclear heat exchange system and evaporator under different operating conditions

    • 摘要: 核能作为安全稳定、低碳高效的优质能源,是构建北方地区清洁取暖体系的理想选择。然而核能供热系统在实际运行中存在明显难题:采暖负荷随气象条件和用户需求频繁波动,反应堆运行特性难以适应负荷变化的动态响应;另一方面非采暖季无需供热导致供热堆被迫停堆,影响系统的运行效率和经济性。因此,为保证核堆安全、稳定、高效运行,设计多套换热器组并联的换热系统,以适配不同负荷工况的运行需求。使用成熟的商业软件Aspen Plus建立换热系统模型,验证不同工况的运行方案;同时使用配套软件Aspen EDR对不同壳侧流量的蒸发器进行模拟计算,获取温度、蒸汽分数、换热系数等参数,分析沿壳体直径方向和沿程方向的变化规律,得到不同工况下蒸发器内部工作情况。结果分析发现:换热器在非设计工况下运行,存在面积余量,导致模拟计算和校核计算存在一定差距。非设计工况的面积余量范围可达-37.96%~64.62%,面积余量为正表示实际换热面积大于所需换热面积,导致热流出口温度更低,冷流出口温度更高,换热器热负荷升高,面积余量为负同理。面积余量过高导致软件警告,进一步对不同工况下蒸发器工作情况模拟分析,发现100%负荷三列运行壳侧流量25kg/s工况下管束区蒸汽分数较高,在Y方向514mm处蒸汽分数达到100%,管束出口区蒸汽过热达到240℃以上,管束过热风险高;提高壳侧流量至26kg/s,壳侧总体温度降低未出现过热蒸汽,管束区蒸汽最高仅8.31%。

       

      Abstract: Nuclear energy, as a high-quality energy source characterized by safety, stability, low carbon emissions, and high efficiency, is considered an ideal choice for constructing a clean heating system in northern regions. However, practical operation of nuclear heating systems faces notable challenges: heating loads fluctuate frequently with weather conditions and user demand, making it difficult for reactor operating characteristics to adapt to the dynamic response of load variations; meanwhile, the lack of heating demand during non-heating seasons forces heating reactors to shut down, compromising system operational efficiency and economy. Therefore, to ensure the safe, stable, and efficient operation of nuclear reactors, a heat exchange system with multiple sets of parallel heat exchanger batteries was designed to accommodate operating requirements under different load conditions. The commercial software Aspen Plus was employed to establish a model of the heat exchange system, verifying operation schemes under various working conditions. Additionally, the supporting software Aspen EDR was used to simulate evaporators under different shell-side flow rates, obtaining parameters such as temperature, vapor fraction, and heat transfer coefficients. Variations along the shell diameter and flow direction were analyzed to understand the internal working conditions of the evaporator under different operational scenarios. Analysis of the results reveals that when heat exchangers operate under off-design conditions, there exists an area margin, leading to a certain discrepancy between simulated and verified calculations. The range of area margin under off-design conditions can reach -37.96% to 64.62%. A positive area margin indicates that the actual heat transfer area exceeds the required area, resulting in lower outlet temperatures of the hot fluid, higher outlet temperatures of the cold fluid, and an increased heat load of the exchanger. Conversely, a negative area margin implies the opposite. Excessively high area margins trigger software warnings. Further simulation analysis of evaporator performance under various conditions showed that under 100% load with three columns in operation and a shell-side flow rate of 25 kg/s, the vapor fraction in the tube bundle zone was relatively high, reaching 100% at 514 mm in the Y-direction. The steam at the tube bundle outlet became superheated, exceeding 240°C, indicating a high risk of tube bundle overheating. When the shell-side flow rate was increased to 26 kg/s, the overall shell-side temperature decreased without generating superheated steam, and the maximum vapor fraction in the tube bundle zone was only 8.31%.

       

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