超临界CO2布雷顿循环PCHE预冷器热工性能分析

Mingjian Lu, Xin-ping Yan, Jian Wang, Yuwei Sun, Zikang Gong
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引用次数: 3

摘要

印刷电路换热器(PCHE)是一种新型的毫米级通道换热器。超临界二氧化碳(SCO2)布雷顿循环PCHE预冷器中的工作流体通常在伪临界点附近或越过伪临界点,其热物理性质表现出强烈的非线性特征。这给PCHE的热水力性能分析带来了挑战。本文采用分段法建立了直通道PCHE预冷器模型,以准确地反映热物性的变化。采用Gnielinski经验关联设计预冷器。分析了SCO2沿长度方向的局部换热和压降特性。结果表明,分段法得到的设计长度明显大于对数平均温差法。总体上,局部温差从热端到冷端逐渐减小。SCO2侧换热系数与普朗特数的关系大于与雷诺数的关系。研究结果对PCHE设计方法的发展具有重要意义。
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Thermal Hydraulic Performance Analysis of PCHE Precooler for Supercritical CO2 Brayton Cycle
Printed circuit heat exchanger (PCHE) is a new type of millimeter–level channel heat exchanger. The working fluid in the PCHE precooler of the supercritical carbon dioxide (SCO2) Brayton cycle usually works near or cross the pseudo-critical point, where the thermophysical properties exhibit drastic nonlinear characteristics. This brings challenges to analysis the thermal hydraulic performance of the PCHE. In present paper, a straight channel PCHE precooler model is established by the segment method to accurately account for the change of thermophysical properties. The precooler is designed by adopting the Gnielinski empirical correlations. Local heat transfer and pressure drop characteristics of SCO2 along the length are analyzed. The results show that the designed length obtained by segment method is significantly larger than by logarithmic mean temperature difference (LMTD) method. Overall the local temperature difference decreases from the hot end to the cold end. The heat transfer coefficient on SCO2 side is more relevant to the Prandtl number than the Reynolds number. The research results are of great significance for the development of PCHE design methods.
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