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Experimental investigation of heat transfer in coiled tube type molten salt steam generator

机译:卷管型熔盐蒸汽发生器传热试验研究

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摘要

Heat transfer performance of coiled tube type molten salt steam generator has been experimentally reported, and the wall temperature distribution, steam generation rate and thermal efficiency were comprehensively investigated. Heat transfer of the system was mainly determined by two phase flow inside coiled tube and molten salt convection outside tube. The coiled tube can be divided into three regions as liquid phase region, vapor-liquid two phase region and superheat steam region, and the wall temperature in two phase region first decreased for nucleate boiling with high heat transfer coefficient and then increased. When molten salt temperature increased, overall heat transfer coefficient and thermal efficiency first increased, and then dropped due to heat transfer deterioration for superheat steam and high heat loss. According to present experimental system, overall heat transfer coefficient had maximum of 290 W/m(2) K at optimal molten salt temperature of 340 degrees C, while thermal efficiency approached to its maximum at molten salt temperature of 320 degrees C. When inlet water flow rate was increased, the superheat gradually decreased with the wall temperature dropping, and the overall heat transfer coefficient, steam generation rate and thermal efficiency first increased and then decreased. Moreover, molten salt forced convection can remarkably improve overall heat transfer coefficient.
机译:经过实验报道了盘管式熔盐蒸汽发生器的传热性能,综合研究了壁温分布,蒸汽发生率和热效率。系统的传热主要由卷轴管和外部熔盐对流内的两个相流决定。卷绕管可以分为三个区域作为液相区域,汽液两相区域和过热蒸汽区域,并且两个相位区域中的壁温首先用于核心沸腾,具有高传热系数,然后增加。当熔融盐温度的增加时,总传热系数和热效率首先增加,然后由于传热劣化而导致过热蒸汽和高热量损失。根据目前的实验系统,总传热系数最大为290W / m(2)k,在340℃的最佳熔融盐温度下,热效率在熔融盐温度下达到320℃的最大值。当入口水时流速增加,过热随着壁温滴加逐渐降低,并且总传热系数,蒸汽发生率和热效率首先增加,然后减少。此外,熔盐强制对流可以显着提高整体传热系数。

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