A novel liquid natural gas combined cycle system integrated with liquid nitrogen energy storage and carbon capture for replacing coal-fired power plants: System modelling and 3E analysis

被引:2
作者
Guo, Wei [1 ,2 ]
Kong, Fulin [1 ]
Shen, Minghai [1 ]
Tong, Lige [1 ,2 ]
Jin, Yi [3 ]
Feng, Wujun [4 ]
Wang, Li [1 ,2 ]
Ding, Yulong [5 ,6 ]
机构
[1] Univ Sci & Technol Beijing, Sch Energy & Environm Engn, Beijing 100083, Peoples R China
[2] Univ Sci & Technol Beijing, Beijing Key Lab Energy Saving & Emiss Reduct Met I, Beijing 100083, Peoples R China
[3] Jiangsu Jinhe Energy Technol Co Ltd, Jurong 212499, Jiangsu, Peoples R China
[4] Beijing Jingneng Energy Technol Res Co Ltd, Beijing 100022, Peoples R China
[5] Univ Birmingham, Birmingham Ctr Energy Storage, Birmingham, England
[6] Univ Birmingham, Sch Chem Engn, Birmingham, England
基金
北京市自然科学基金;
关键词
Liquefied natural gas; Liquid nitrogen energy storage; Integrated system; Power peak regulation; Thermodynamic analysis; LNG COLD ENERGY; THERMODYNAMIC ANALYSIS; RANKINE-CYCLE; REGASIFICATION; FUEL; OPTIMIZATION; DESIGN; HEAT;
D O I
10.1016/j.enconman.2023.117755
中图分类号
O414.1 [热力学];
学科分类号
摘要
The judicious utilization of cryogenic energy released during the regasification process of liquid natural gas (LNG) is important for enhancing the operational efficiency of combined-cycle power plants utilizing LNG. This study introduces an innovative natural gas combined cycle (NGCC) process, denoted as NGCC-LNES, designed for power generation and carbon capture through the utilization of LNG cryogenic energy, specifically targeting the alleviation of the load on conventional coal-fired peak-shaving power plants. The proposed process lowers the boiling point of liquid nitrogen below the LNG storage temperature through nitrogen pressurization. Subsequently, the cold energy inherent in LNG is harnessed to liquefy nitrogen, and the surplus cold energy is stored for the continuous liquefaction of CO2. Illustrating this concept with an NGCC system featuring a 1 kg/s LNG flow rate, we developed a numerical calculation model employing Aspen Plus for a comprehensive analysis encom-passing energy, exergy, and power peak regulation. Furthermore, this study conducts an in-depth examination of the influence exerted by the peak-to-valley power-price ratio on the payback period of the system. It also explores the prospective applications of this innovative system in China and other major LNG-importing nations world-wide as a replacement for peak-shaving coal-fired power plants. The results show that over a 24-hour operational period, the LNES system can consistently and reliably supply 2722.82 kW of power for 8 h, achieving a round-trip efficiency of 75.26 %. Specifically, the exergy efficiencies of the NGCC-LNES during the energy storage and release phases are determined as 58.50 % and 54.44 %, respectively. Notably, as the peak-to-valley power price ratio escalates from 2.5 to 5, the payback period of the system investment contracts significantly, decreasing from 24.62 years to 4.25 years. Remarkably, the initial investment cost of the LNES technology stands at 947.58 $/kW, positioning it competitively relative to alternative energy storage technologies such as compressed air, sodium-sulfur batteries, and flow batteries, and closely aligns with pumped hydro energy storage solutions. Importantly, this innovative technology has the capacity to reduce carbon emissions by 0.21 % and 1.5 % for major global LNG importers by 2022 and China by 2060, respectively.
引用
收藏
页数:12
相关论文
共 37 条
  • [1] Reduction of efficiency penalty for a natural gas combined cycle power plant with post-combustion CO2 capture: Integration of liquid natural gas cold energy
    Bao, Junjiang
    Zhang, Lei
    Song, Chunxiao
    Zhang, Ning
    Guo, Minggang
    Zhang, Xiaopeng
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2019, 198
  • [2] Strengthening power generation efficiency utilizing liquefied natural gas cold energy by a novel two-stage condensation Rankine cycle (TCRC) system
    Bao, Junjiang
    Lin, Yan
    Zhang, Ruixiang
    Zhang, Ning
    He, Gaohong
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2017, 143 : 312 - 325
  • [3] A review on liquid air energy storage: History, state of the art and recent developments
    Borri, Emiliano
    Tafone, Alessio
    Romagnoli, Alessandro
    Comodi, Gabriele
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2021, 137 (137)
  • [4] Oxy-fuel combustion technology for coal-fired power generation
    Buhre, BJP
    Elliott, LK
    Sheng, CD
    Gupta, RP
    Wall, TF
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2005, 31 (04) : 283 - 307
  • [5] Analysis and optimization of cascade Rankine cycle for liquefied natural gas cold energy recovery
    Choi, In-Hwan
    Lee, Sangick
    Seo, Yutaek
    Chang, Daejun
    [J]. ENERGY, 2013, 61 : 179 - 195
  • [6] Couper J.R., 2012, Chemical Process Equipment, VThird, P731, DOI DOI 10.1016/B978-0-12-396959-0.00021-5
  • [7] THERMODYNAMIC ANALYSIS OF RE-GASIFICATION OF LNG FOR DESALINATION OF SEA-WATER
    CRAVALHO, EG
    MCGRATH, JJ
    TOSCANO, WM
    [J]. CRYOGENICS, 1977, 17 (03) : 135 - 139
  • [8] [Du Qiang 杜强], 2015, [Journal of Resources and Ecology, 资源与生态学报], V6, P318
  • [9] Thermodynamic analysis for working fluids comparison in Rankine-type cycles exploiting the cryogenic exergy in Liquefied Natural Gas (LNG) regasification
    Ferreira, P. A.
    Catarino, I.
    Vaz, D.
    [J]. APPLIED THERMAL ENGINEERING, 2017, 121 : 887 - 896
  • [10] Combined cascaded Rankine and direct expander based power units using LNG (liquefied natural gas) cold as heat sink in LNG regasification
    Ferreiro Garcia, Ramon
    Carbia Carril, Jose
    Romero Gomez, Javier
    Romero Gomez, Manuel
    [J]. ENERGY, 2016, 105 : 16 - 24