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    燃气轮机进气深度冷却换热器设计和性能分析研究

    Design and CFD-Based Optimization of a Deep-Cooling Heat Exchanger for Gas Turbine Inlet Air

    • 摘要: 针对大型燃气轮机进气深度冷却换热器一维设计难以反映三维流动、全尺寸CFD计算成本高的问题,构建了理论设计—局部CFD校核—综合评价方法,比较光管错排、翅片圆管顺排、翅片圆管错排和翅片椭圆管错排四种结构。以空气由40℃冷却至15℃为目标,采用LMTD与分布参数模型确定初始尺寸;沿流向划分四个区段,在截面选取中心、中上、中侧和角部区域开展局部CFD,并以面积加权重构整体出口温度与压降。结果表明,四种结构CFD出口温度相对理论值的偏差依次为−8.41%、7.24%、2.08%和10.66%。翅片圆管顺排结构压降最低,为152.6Pa;翅片椭圆管错排结构体积最小,为221.2m3,其Q/V最高,达到7.46×104W·m-3,Q/ΔP为1.03×105W·Pa-1,仅比顺排结构低5.6%。错排圆管强化横向掺混与尾迹干涉,但增大流动阻力;椭圆管可缩小低速尾迹区,兼顾紧凑性与低阻。综合比较,翅片椭圆管错排结构具有较优综合性能,可为大型燃气轮机进气冷却换热器选型提供参考。

       

      Abstract: A methodology combining theoretical design, local CFD validation, and comprehensive evaluation was developed for large gas-turbine inlet deep-cooling heat exchangers. Four configurations were compared: staggered bare tubes, in-line circular finned tubes, staggered circular finned tubes, and staggered finned elliptical tubes. The initial dimensions were determined using the LMTD method and a distributed-parameter model to cool air from 40℃ to 15℃. Local CFD simulations were performed in four axial sections and four representative cross-sectional regions, and the overall outlet temperature and pressure drop were reconstructed by area-weighted averaging.The CFD outlet temperatures deviated from the theoretical values by−8.41%, 7.24%, 2.08%, and 10.66%, respectively. The in-line finned-tube configuration had the lowest pressure drop of 152.6 Pa. The staggered finned elliptical-tube configuration achieved the smallest volume of 221.2 m3, the highest Q/V of 7.46×104W·m-3, and a Q/ΔP of 1.03×105W·Pa-1, only 5.6% lower than that of the in-line configuration. Overall, this configuration provided the best balance among heat-transfer performance, compactness, and flow resistance.

       

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