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Numerical investigation on the mixed convection and heat transfer of supercritical water in horizontal tubes in the large specific heat region

机译:大比热区水平管中超临界水混合对流换热的数值研究

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Numerical simulation is performed in the present study to get further insight into the mechanism of heat transfer phenomena of water in 032 × 3 mm horizontal smooth tubes under supercritical pressures. Both the heat transfer enhancement (HTE) and heat transfer deterioration (HTD) in the so-called large specific heat region (LSHR) of supercritical fluids are analyzed based on the numerical results. The governing equations of the fluid are solved on fixed three-dimensional grid systems, and the RNG-k-ε model with enhanced wall treatment method is employed to handle the coupled wall-to-fluid heat transfer. The numerical results are compared with the corresponding experimental data, and a good agreement is achieved, indicating good accuracy and reliability of the numerical method used in this study. Variation of the tube inner wall temperature and the local heat transfer coefficient with a few parameters, such as the local water enthalpy, the water mass flow rate and the heat flux on the tube wall, are obtained under various conditions. It is showed that in the large specific heat region (LSHR), there exists strong non-uniformity in the circumferential distribution of the tube inner wall temperature, and as well, the heat flux on the inner tube wall are distinctly non-uniform along the tube wall circumference. Further analysis of the numerical data shows that the above-mentioned non-uniformity is mainly due to the rapid change in fluid properties, which results complex secondary flows and mixed convection in the supercritical fluid. Based on the numerical results, a critical value is obtained for the parameter Gr/Re~(2.7), which is believed to be a key parameter affecting the secondary flow in the LSHR. In the present study, the critical value for Gr/Re~(2.7) is determined to be 1.5×10~(-5), above which the HTD phenomenon may be observed.
机译:在本研究中进行了数值模拟,以进一步了解在超临界压力下032×3 mm水平光滑管中水的传热现象机理。基于数值结果,分析了所谓的超临界流体大比热区(LSHR)中的传热增强(HTE)和传热劣化(HTD)。在固定的三维网格系统上求解了流体的控制方程,并采用带有增强壁处理方法的RNG-k-ε模型来处理壁-流体耦合传热。将数值结果与相应的实验数据进行比较,取得了很好的一致性,表明本研究中使用的数值方法具有良好的准确性和可靠性。在各种条件下,可以获得管内壁温度和局部传热系数随一些参数的变化,例如局部水焓,水质量流量和管壁上的热通量。结果表明,在较大的比热区(LSHR)中,管内壁温度的周向分布存在很强的不均匀性,并且沿管壁的内管壁上的热通量也明显不均匀。管壁周长。数值数据的进一步分析表明,上述不均匀性主要归因于流体性质的快速变化,这导致了超临界流体中复杂的二次流和混合对流。根据数值结果,获得参数Gr / Re〜(2.7)的临界值,该临界值被认为是影响LSHR中二次流的关键参数。在本研究中,将Gr / Re〜(2.7)的临界值确定为1.5×10〜(-5),在此之上可以观察到HTD现象。

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