Peak-Shaving of the Oxy-Fuel Power Plant Coupled with Liquid O2 Storage

被引:0
|
作者
Fu, Xuchen [1 ,2 ]
Wu, Jianwen [1 ]
Sun, Zhenkun [1 ]
Duan, Yuanqiang [1 ]
Gao, Zhengping [2 ]
Duan, Lunbo [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Key Lab Energy Thermal Convers & Control, Minist Educ, Nanjing 210096, Peoples R China
[2] Inner Mongolia Power Grp Co Ltd, Inner Mongolia Power Res Inst Branch, Hohhot 010020, Peoples R China
关键词
oxy-fuel; peak-shaving; liquid O-2 storage; cold energy recovery; ENERGY-STORAGE; CO2; CAPTURE; THERMODYNAMIC ANALYSIS; COMBUSTION; EXERGY; SYSTEM; COST; TECHNOLOGIES; SIMULATION; CYCLE;
D O I
10.1007/s11630-023-1864-1
中图分类号
O414.1 [热力学];
学科分类号
摘要
Integrating a high proportion of intermittent renewable energy provides a solution for the higher peak-shaving capacity of coal-fired power plants. Oxy-fuel combustion is one of the most promising carbon reduction technologies for coal-fired power plants. This study has proposed a novel oxy-fuel power plant that is coupled with both liquid O-2 storage and cold energy recovery systems in order to adapt to the peak-shaving requirements. The liquid O-2 storage system uses cheap valley electricity to produce liquid O-2 for a later use in the peak period to enhance the peak-shaving capacity. Meanwhile, the cold energy recovery system has been introduced to recover the physical latent energy during the phase change of liquid O-2 to increase the power generation in the peak period. Technical economies of three power plants, i.e. a 330 MW (e) oxy-fuel power plant as reference (Case 1), the same power plant coupled with only liquid O-2 storage system (Case 2), and the same power plant coupled with both liquid O-2 storage and cold energy recovery systems (Case 3), have been analyzed and compared. Thermodynamic performance analysis indicates that the peaking capacity of Case 3 can reach the range of 106.03 to 294.22 MW (e), and the maximum peak-shaving coefficient can be as high as 2.77. Exergy analysis demonstrates that the gross exergy efficiency of Cases 2 and 3 reaches 32.18% and 33.57%, respectively, in the peak period, which are significantly higher than that of 26.70% in Case 1. Economic analysis shows that through selling the liquid O-2 and liquid CO2, combined with carbon trading, the levelized cost of electricity (LCOE) of the three cases have been greatly reduced, with the lowest one of 30.90 USD/MWh shown in Case 3. For a comprehensive consideration, Case 3 can be considered a future reference of oxy-fuel power plant with the best thermodynamic and economic performance.
引用
收藏
页码:1722 / 1736
页数:15
相关论文
共 50 条
  • [41] Flue gas recovery system for natural gas combined heat and power plant with distributed peak-shaving heat pumps
    Zhao, Xiling
    Fu, Lin
    Wang, Xiaoyin
    Sun, Tao
    Wang, Jingyi
    Zhang, Shigang
    APPLIED THERMAL ENGINEERING, 2017, 111 : 599 - 607
  • [42] Pulverized combustion under conventional (O2/N2) and oxy-fuel (O2/CO2) conditions of biomasses treated at different temperatures
    Pohlmann, Juliana G.
    Osorio, Eduardo
    Vilela, Antonio C. F.
    Diez, Maria Antonia
    Borrego, Angeles G.
    FUEL PROCESSING TECHNOLOGY, 2017, 155 : 174 - 182
  • [43] Economic Dispatch of High-proportion Renewable Energy Power System Considering Peak-shaving Compensation of Concentrating Solar Power Plant
    Cui Y.
    Yu S.
    Zhang J.
    Wang M.
    Wang X.
    Fu G.
    Zhongguo Dianji Gongcheng Xuebao/Proceedings of the Chinese Society of Electrical Engineering, 2023, 43 (13): : 4922 - 4934
  • [44] Flamelet LES of oxy-fuel swirling flames with different O2/CO2 ratios using directly coupled seamless multi-step solid fuel kinetics
    Nicolai, Hendrik
    Debiagi, Paulo
    Janicka, Johannes
    Hasse, Christian
    FUEL, 2023, 344
  • [45] Hybrid power plant for energy storage and peak shaving by liquefied oxygen and natural gas
    Barsali, Stefano
    Ciambellotti, Alessio
    Giglioli, Romano
    Paganucci, Fabrizio
    Pasini, Gianluca
    APPLIED ENERGY, 2018, 228 : 33 - 41
  • [46] Effect of the impurities O2 or NO present in non-purified flue gas from oxy-fuel combustion processes for carbon capture and storage technology
    Melendo, Ana Pilar
    Berbes, Roberto
    Blanco, Sofia T.
    Fernandez, Javier
    PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2023, 172 : 1120 - 1131
  • [47] Techno-economic analysis of oxy-fuel power plant for coal and biomass combined with a power-to-gas plant
    Sohn, Geun
    Ryu, Ju-yeol
    Park, Hyemin
    Park, Sungho
    ENERGY FOR SUSTAINABLE DEVELOPMENT, 2021, 64 : 47 - 58
  • [48] Synergistic Removal of SOx and NOx in CO2 Compression and Purification in Oxy-Fuel Combustion Power Plant
    Wu, Haibo
    Chen, Wei
    Wu, Jinhua
    Zheng, Zhimin
    Duan, Lunbo
    ENERGY & FUELS, 2019, 33 (12) : 12621 - 12627
  • [49] Simulation of O2/N2 behaviors on multi-component polymeric membranes in oxy-fuel combustion system
    Wang, Lize
    Zhong, Wenqi
    Yu, Aibing
    POWDER TECHNOLOGY, 2023, 419
  • [50] Evaluating the influence of H2O phase state on the performance of LNG oxy-fuel combustion power plant: Exergy and exergoeconomic analyses
    Cai, Lei
    Fu, Yidan
    Cheng, Zeyang
    Tan, Liping
    Guan, Yanwen
    Liu, Wenbin
    APPLIED THERMAL ENGINEERING, 2022, 204