混合工质对sCO2布雷顿循环热效率与高点压力的协同提升机制
Synergistic Enhancement Mechanism of Mixed Working Fluids on Thermal Efficiency and Peak Pressure in sCO2 Brayton Cycles
DOI: 10.12677/se.2025.156011, PDF,   
作者: 王 伟, 许鲁丰, 吴玉庭:北京工业大学机械与能源工程学院,北京;传热与能源利用北京市重点实验室,北京
关键词: sCO2布雷顿循环混合工质热效率系统压力sCO2 Brayton Cycle Mixed Working Fluid Thermal Efficiency System Pressure
摘要: 超临界二氧化碳(sCO2)布雷顿循环因高热效率和紧凑性被广泛关注,但其依赖纯CO2工质需在高温高压(临界点304.13 K/7.39 MPa)下运行,导致设备成本高且热源适配性受限。针对此问题,本研究通过热力学建模与数值模拟,系统研究了乙烷、丙烷、R116等低浓度(0~10 mol%)混合工质对sCO2循环热效率与系统高点压力的协同调控作用,明确了工质临界参数对循环性能的调控规律。结果表明,丙烷在800 K工况下既能使热效率提升2.5%,又能降低系统高点压力15.2%,在效率–压力权衡中表现最优;R116和R125则分别适用于效率优先与压力敏感场景。该研究为sCO2循环在核能、太阳能热发电等领域的高效低碳运行提供了明确的工质选型策略,拓展了混合工质调控技术的应用边界。
Abstract: The supercritical carbon dioxide (sCO2) Brayton cycle has attracted extensive attention due to its high thermal efficiency and compactness. However, its reliance on pure CO2 as working fluid requires operation under high temperature and pressure conditions (critical point: 304.13 K/7.39 MPa), leading to elevated equipment costs and restricted thermal source compatibility. To address these challenges, this study systematically investigates the synergistic regulation effects of low-concentration (0~10 mol%) mixed working fluids (ethane, propane, R116) on thermal efficiency and peak system pressure of sCO2 cycles through thermodynamic modeling and numerical simulations. The regulatory mechanisms of working fluid critical parameters on cycle performance are elucidated. Results demonstrate that propane achieves optimal trade-off performance under 800 K operating conditions, simultaneously improving thermal efficiency by 2.5% and reducing peak system pressure by 15.2%. R116 and R125 are respectively recommended for efficiency-prioritized and pressure-sensitive scenarios. This research provides clear working fluid selection strategies for efficient and low-carbon operation of sCO2 cycles in nuclear energy and solar thermal power generation applications, thereby expanding the application boundaries of mixed working fluid regulation technology.
文章引用:王伟, 许鲁丰, 吴玉庭. 混合工质对sCO2布雷顿循环热效率与高点压力的协同提升机制[J]. 可持续能源, 2025, 15(6): 93-105. https://doi.org/10.12677/se.2025.156011

参考文献

[1] Agency, I.E. (2024) World Energy Outlook 2024. IEA.
[2] Zheng, N., Li, Z., Fang, J. and Wei, J. (2023) Supercritical CO2 Mixture Brayton Cycle with Floating Critical Points for Concentrating Solar Power Application: Concept and Thermodynamic Analysis. Energy Conversion and Management, 284, Article 116989. [Google Scholar] [CrossRef
[3] Teja, D.V.H., Muvvala, P., Prashanth Nittala, N.A., Bandhu, D., Khan, M.I., Saxena, K.K., et al. (2024) Comparative Performance Analysis of Recuperative Helium and Supercritical CO2 Brayton Cycles for High-Temperature Energy Systems. Energy, 312, Article 133469. [Google Scholar] [CrossRef
[4] Wang, X., Zhang, L., Zhu, Z., Hu, M., Wang, J. and Fan, X. (2023) Performance Improvement Overview of the Supercritical Carbon Dioxide Brayton Cycle. Processes, 11, Article 2795. [Google Scholar] [CrossRef
[5] Jeong, W.S. and Jeong, Y.H. (2013) Performance of Supercritical Brayton Cycle Using CO2-Based Binary Mixture at Varying Critical Points for SFR Applications. Nuclear Engineering and Design, 262, 12-20. [Google Scholar] [CrossRef
[6] Guo, J.Q., Li, M.J., He, Y.L., et al. (2019) A Study of New Method and Comprehensive Evaluation on the Improved Performance of Solar Power Tower Plant with the CO2-Based Mixture Cycles. Applied Energy, 256, Article 113837. [Google Scholar] [CrossRef
[7] Hu, L., Chen, D., Huang, Y., Li, L., Cao, Y., Yuan, D., et al. (2015) Investigation on the Performance of the Supercritical Brayton Cycle with CO2-Based Binary Mixture as Working Fluid for an Energy Transportation System of a Nuclear Reactor. Energy, 89, 874-886. [Google Scholar] [CrossRef
[8] Binotti, M., Invernizzi, C.M., Iora, P. and Manzolini, G. (2019) Dinitrogen Tetroxide and Carbon Dioxide Mixtures as Working Fluids in Solar Tower Plants. Solar Energy, 181, 203-213. [Google Scholar] [CrossRef
[9] Zhou, Y., Yin, D., Guo, X. and Dong, C. (2022) Numerical Analysis of the Thermal and Hydraulic Characteristics of CO2/Propane Mixtures in Printed Circuit Heat Exchangers. International Journal of Heat and Mass Transfer, 185, Article 122434. [Google Scholar] [CrossRef
[10] 乔加飞, 李卓, 廖海燕, 等. 超临界二氧化碳循环混合工质热力学性质研究进展[J]. 热力发电, 2022, 51(9): 1-10.
[11] Sun, R., Wang, J., Tian, H. and Shu, G. (2024) Critical Points Calculation of CO2-Based Binary Mixture Working Fluids: Evaluation of PC-SAFT Equation of State. Fluid Phase Equilibria, 577, 113986. [Google Scholar] [CrossRef
[12] Lemmon, E.W., Bell, I.H., Huber, M.L., et al. (2018) NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 10.0. National Institute of Standards and Technology.
[13] Wright, S.A., Conboy, T.M., Parma, E.J., et al. (2011) Summary of the Sandia Supercritical CO2 Development Program. Chinese Journal of Chemistry, 19, 1562-1564.