首页|变截面耦合通道PCHE内超临界CO2热工水力性能研究

变截面耦合通道PCHE内超临界CO2热工水力性能研究

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本文采用数值模拟方法,以超临界CO2(S-CO2)作为印刷电路板式换热器(Printed Circuit Heat Exchanger,PCHE)冷、热两侧耦合换热的流体,对圆形等截面耦合通道、圆形渐扩截面耦合通道以及圆形渐缩截面耦合通道的热工水力性能进行了对比研究。研究结果表明,在相同换热面积下,相较于传统等截面通道PCHE,S-CO2在冷热两侧均为渐缩通道的PEC均大于1,最大达到了 2。16,最小则为1。38,其综合性能最优。然而,S-CO2在两侧均为渐扩通道的PEC均小于,综合性能较差。降低冷侧运行压力有利于提高渐缩通道的综合性能。研究结果为PCHE的设计提供了新的思路和理论指导。
Study on Thermal and Hydraulic Performance of Supercritical CO2 in Coupled Channel PCHE With Variable Cross-section
In this paper,using S-CO2 as the heat transfer fluid on the cold and hot sides of the Printed Circuit Heat Exchanger(PCHE),the thermal and hydraulic performance of the circular constant cross section coupling channel,the circular diverging channel and the circular converging channel were compared by numerical simulation method.The results show that,under the same heat transfer area,compared with the traditional constant cross section channel PCHE,the PEC of S-CO2 in the converging channel on both hot and cold sides is greater than 1,the maximum reaches 2.16,and the minimum is 1.38,which shows the best comprehensive performance.However,the PEC of S-CO2 in both sides of the diverging channel is less than 1,and the overall performance is poor.Decreasing the cold side operating pressure is beneficial to improve the comprehensive performance of the converging channel.The results provide new ideas and theoretical guidance for the design of PCHE.

supercritical carbon dioxidePCHEvariable cross section channelthermal and hy-draulic performance

朱兵国、何吉祥

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兰州理工大学机电工程学院,兰州 730050

超临界二氧化碳 PCHE 变截面通道 热工水力性能

甘肃省青年科技项目兰州理工大学红柳优秀青年基金

22JR5RA28307-062310

2024

工程热物理学报
中国工程热物理学会 中国科学院工程热物理研究所

工程热物理学报

CSTPCD北大核心
影响因子:0.4
ISSN:0253-231X
年,卷(期):2024.45(6)
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