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Numerical modelling of a parallel flow heat exchanger with two-phase heat transfer process

机译:双相传热过程平行流动热交换器的数值模型

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In this analysis a 1-D steady state heat transfer was accomplished for tube and shell type heat exchanger with parallel flow configuration. Molten salt was regarded as a secondary flow that runs in the shell part of the heat exchanger whereas the saturated water was regarded as the primary flow that flows in the tube part of heat exchanger. The analysis is done for 0.1 kg/s mass flow rate of the primary flow and for various mass flow rate of the secondary flow ranging from 0.1 kg/s to 0.6 kg/s. The heat exchanger's thermal characteristics, such as, variation in steam quality and two-phase convective coefficient of the saturated water alongside the length of the tube are collected from the analysis. In addition, temperature profiles for primary and secondary flows are presented in this article. It is found that for the considered geometry of the heat exchanger and the boundary conditions, a 0.376 kg/s mass flow rate of molten salt is required to convert the 0.1 kg/s mass flow rate of primary flow into saturated steam. As a result, a mass flow rate of molten salt which is greater than 0.376 kg/s is required to super heat the primary fluid (water).
机译:在该分析中,具有具有平行流动配置的管和壳式热交换器的1-D稳态传热。熔融盐被认为是在热交换器的壳体部分中运行的二次流动,而饱和水被认为是在热交换器的管部分中流动的主要流动。该分析是针对主要流动的0.1kg / s质量流量的0.1kg / s质量流速,并且用于从0.1kg / s的次流量的各种质量流量为0.6kg / s。从分析中收集热交换器的热特性,例如蒸汽质量和饱和水的两相对流系数的变化。此外,本文提出了用于初级和二次流动的温度曲线。结果发现,对于热交换器和边界条件的考虑几何形状,需要熔盐的0.376kg / s质量流速,将0.1kg / s质量流速转化为饱和蒸汽。结果,需要大于0.376kg / s的熔盐的质量流速来超越主要流体(水)。

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