氟盐冷却高温先进反应堆全板横流和逆流印刷电路换热器迭代算法研究

Xinze Li, Dalin Zhang, Xinyu Li, Wenxi Tian, Suizheng Qiu, G.H. Su
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引用次数: 1

摘要

在氟盐冷却高温高级反应器(FuSTAR)的概念中,印刷电路换热器(PCHE)主要考虑在其超临界二氧化碳(S–CO2)布雷顿循环二次回路中。PCHE的设计基于布雷顿循环系统设计提供的工作流体的性质。因此,需要一种快速迭代的PCHE设计方法。在本研究中,提出了一个基于Picard迭代方法的数学模型。该模型可以并行求解具有复杂边界条件和初始值的全板温度场,包括横流和逆流PCHE。基于FuSTAR布雷顿循环设计条件,利用数学模型分别模拟了三种尺寸的横流和逆流PCHEs。与计算流体动力学(CFD)模型、一维和三维耦合模型和三维模型相比,该数学模型将计算时间从1到10小时缩短到1到10秒,由于边缘效应和局部扰动,最小尺寸情况下的最大温度平均偏差为18.6%,而其他尺寸情况下为8.4%。以二回路回热器设计为例,数学模型的计算速度和精度均能满足FuSTAR PCHE的设计要求。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Study on iterative algorithm of full plate cross-flow and counter-flow printed circuit heat exchanger for fluoride-salt-cooled high-temperature advanced reactor

In the concept of Fluoride-Salt-cooled high-Temperature Advanced Reactor (FuSTAR), the Printed Circuit Heat Exchanger (PCHE) is mainly considered in its supercritical carbon dioxide (S–CO2) Brayton cycle secondary loop. The design of the PCHE is based on the property of working fluid provided by the Brayton cycle system design. Therefore, a fast and iterative PCHE design method is required. In this study, a mathematical model based on Picard's iterative method is proposed. The model can solve full plate temperature field with complex boundary conditions and initial values including cross-flow and counter-flow PCHE in parallel. Based on FuSTAR Brayton cycle design conditions, three sizes of cross-flow and counter-flow PCHEs are simulated respectively by the mathematical model. Compared with Computational Fluid Dynamics (CFD) models, a one and three-dimensional coupling model and a three-dimensional model, the mathematical model reduced the computing time from 1 to 10 h to 1–10 s, and the maximum temperature mean deviation is 18.6% for the smallest size case because of the edge effect and local disturbance, but 8.4% for other size. Taking secondary loop recuperator design as example, the computing speed and accuracy of the mathematical model can meet the design requirements of FuSTAR PCHE.

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