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Experimental investigation on the shell-side heat transfer performance of molten salt steam generator

机译:熔盐蒸汽发生器壳侧传热性能的实验研究

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In this study, an experiment was conducted to obtain the heat flux and heat transfer coefficient of a mixed molten salt (60% NaNO_3, 40% KNO_3) and water at subcritical pressure in a tube in tube heat exchanger. The control variable method was used in this study. The experimental parameters included the molten salt and water mass fluxes of 38.7-54.1 kg/m~2s and 212.8-259.6 kg/m~2s, respectively, water pressure of 15-19 MPa, water and molten salt inlet temperatures of 200-400 °C and 440-500 °C, respectively, and heat flux of 12-160 kW/m~2. The heat transfer performances of the molten salt and water in the sub-cooled, subcooled boiling, saturated boiling, dryout and superheated regions were analysed with respect to the molten salt and water mass flow rate, inlet salt temperature, water pressure, and inlet water temperature. The fitting correlation of the thermal performance of molten salt to the subcooled boiling or vapor-liquid two-phase flow was presented; the fitting values demonstrated good consistency with the experimental data, with a maximum deviation of -6% and +8%.
机译:在该研究中,进行实验以在管式热交换器中的管中的亚临界压力下获得混合熔盐(60%NaNO_3,40%KnO_3)和水的热通量和热传递系数。本研究使用控制变量方法。实验参数包括熔盐和水质量助熔剂38.7-54.1kg / m〜2s和212.8-259.6 kg / m〜2s,水压为15-19mPa,水和熔盐的盐水温度为200-400 °C和440-500°C,分别为12-160 kW / m〜2的热通量。相对于熔盐和水质流量,入口盐温,水压和入口水,分析了亚冷,过冷沸腾,饱和沸腾,饱和沸点,干燥和过热区域中熔盐和水的热传递性能温度。施用熔盐热性能与过冷沸腾沸腾或汽液两相流的拟合相关性;拟合值与实验数据表现出良好的一致性,最大偏差为-6%和+ 8%。

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