一种可扩展的紧凑型添加剂制造的熔融盐-超临界二氧化碳热交换器,用于太阳能热应用

Ines-Noelly Tano, E. Rasouli, Tracey Ziev, Junwon Seo, Nicholas Lamprinakos, Parth Vaishnav, A. Rollett, Ziheng Wu, V. Narayanan
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引用次数: 0

摘要

介绍了一种用于太阳能热发电的熔融盐/超临界二氧化碳(sCO2)紧凑型主热交换器(PHE)。PHE设计用于处理MS侧高达720°C的温度和sCO2侧200 bar的内部压力。在PHE的核心,MS通过三维周期性晶格网络流动,而sCO2在引脚阵列内流动。PHE设计包括位于MS流内的集成sCO2头,允许PHE的逆流设计。通过有限元模拟确定核心部分内部特征的尺寸,并以优化每个sCO2板中的流动分布和最小化MS侧阻塞的方式配置集管。热交换器的整体设计允许AM水平和垂直的可扩展性,由于集成的头部架构。详细介绍了结构和热流体设计。建立了一个实验验证的、基于相关性的截面PHE核心模型,研究了流动和几何参数对PHE性能的影响,参数包括sCO2和MS侧的质量流量、通道宽度以及PHE的总高度、宽度和长度。模型结果表明,当Cr比为0.8时,换热器的功率密度为18.6 MW/m3(含sCO2容积),效率为0.88。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A Scalable Compact Additively-Manufactured Molten-Salt to Supercritical Carbon Dioxide Heat Exchanger for Solar Thermal Application
An additively-manufactured molten salt (MS) to supercritical carbon dioxide (sCO2) compact primary heat exchanger (PHE) for solar thermal power generation is presented in this paper. The PHE is designed to handle temperatures up to 720 °C on the MS side and an internal pressure of 200 bar on the sCO2 side. Within the core of the PHE, MS flows through a three-dimensional periodic lattice network, while sCO2 flows within pin arrays. The PHE design includes integrated sCO2 headers located within the MS flow, allowing for a counter flow design of the PHE. The dimensions of the internal features of the core section are determined through finite element simulations and the headers are configured in a way that optimizes the flow distribution in each sCO2 plate and minimizes obstruction of the MS side. The overall design of the heat exchanger allows AM scalability both horizontally and vertically due to an integrated header architecture. Details of structural and thermofluidic design are presented. An experimentally-validated, correlation-based sectional PHE core model is developed to study the impact of flow and geometrical parameters on the PHE performance, with varied parameters including the mass flow rate of sCO2 and MS sides, the channels width, and the PHE overall height, width, and length. The model results show that a heat exchanger with a power density of 18.6 MW/m3 (including sCO2 header volume) and effectiveness of 0.88 can be designed achievable at a Cr ratio of 0.8.
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