Centrifugal Pressurization Process in the Near Critical Region for Supercritical CO2 Brayton Cycle

  • SHI Weixiu ,
  • JI Xueyuan ,
  • PAN Lisheng ,
  • SUN Yin ,
  • LI Chaoqi ,
  • WEI Xiaolin
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  • 1. School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing 100044, China 
    2. State Key Laboratory of High Temperature Gas Dynamics, Institute of Mechanics, Chinese Academy of Sciences, Beijing 100190, China

网络出版日期: 2025-09-01

基金资助

Projects (51776215 and 12372237) supported by National Natural Science Foundation of China are gratefully acknowledged.

版权

Science Press, Institute of Engineering Thermophysics, CAS and Springer-Verlag GmbH Germany, part of Springer Nature 2025

Centrifugal Pressurization Process in the Near Critical Region for Supercritical CO2 Brayton Cycle

  • SHI Weixiu ,
  • JI Xueyuan ,
  • PAN Lisheng ,
  • SUN Yin ,
  • LI Chaoqi ,
  • WEI Xiaolin
Expand
  • 1. School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing 100044, China 
    2. State Key Laboratory of High Temperature Gas Dynamics, Institute of Mechanics, Chinese Academy of Sciences, Beijing 100190, China

Online published: 2025-09-01

Supported by

Projects (51776215 and 12372237) supported by National Natural Science Foundation of China are gratefully acknowledged.

Copyright

Science Press, Institute of Engineering Thermophysics, CAS and Springer-Verlag GmbH Germany, part of Springer Nature 2025

摘要

超临界CO2布雷顿循环的增压过程起始于近临界区,若入口压强出现波动,可能会引起增压设备内工质液化和液击现象。基于离心式增压热力过程,考察了不同增压起始压强和温度时离心式增压过程中热力状态点的特性规律,并提出,采用了一种利用焓差和㶲差来表征考察状态点与“发生相变的增压起始区”的距离,可为循环工况优化设计提供可视化参考。结果表明,增压起始于近临界状态时,增压易引起液化;当入口压力为7.4 MPa,温度32°C时,工质处于临界附近,其焓值在405~410 kJ/kg之间,极易在叶轮入口发生相变,液锤风险显著增加;当入口状态点与红区边界点的焓差与㶲差小于5 kJ/kg时,液化趋势显著增强,液锤现象更容易发生;功耗分析表明,比容与压差的增大共同导致功耗上升,恒定出口压24 MPa下的等熵效率可达67%,高于恒定压比工况,内效率可达72%;建议入口温度保持在34°C以上,焓差超过8 kJ/kg,以避开相变风险区,兼顾系统效率与运行安全。此研究为近临界区CO2增压过程优化和关键部件研制提供了重要参考。

本文引用格式

SHI Weixiu , JI Xueyuan , PAN Lisheng , SUN Yin , LI Chaoqi , WEI Xiaolin . Centrifugal Pressurization Process in the Near Critical Region for Supercritical CO2 Brayton Cycle[J]. 热科学学报, 2025 , 34(5) : 1912 -1924 . DOI: 10.1007/s11630-025-2188-0

Abstract

The starting point for the pressurization process of a supercritical CO2 Brayton cycle is near the critical point, which may lead to a liquid hammer if the inlet pressure fluctuates. It is important to judge whether the phase change of working fluid occurs during the pressurization process. With CO2 as the working fluid, the pressurization process for a centrifugal pressurization component is attention considered and analyzed. Specifying the inlet temperature, inlet pressure and outlet pressure as 32°C, 7.4 MPa and 24 MPa, respectively, the thermodynamic parameters of key state points of a centrifugal pressurization component are obtained. At the entrance of the impeller, a phase change of CO2 may occur, especially when the inlet points are close to the critical point. A method using enthalpy difference and exergy difference to express the possibility CO2 phase change is proposed. Furthermore, the risk degree of CO2 phase change is represented visibly. In view of the power consumption and efficiency of compressors under different working conditions, the changes of power consumption, isentropic efficiency and internal efficiency of compression components were analyzed under the conditions of constant outlet pressure and constant pressurization ratio. The power consumption is affected by the specific volume of the working fluid and the pressure difference. With the same inlet conditions, the isentropic efficiency under constant pressurization ratio is higher than that under a constant outlet pressure due to the lower power consumption; the internal efficiency is higher than the isentropic efficiency, and the trend is similar. This method can contribute to the setting of safe conditions for pressurization components.

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