Thermo-economic analysis of SOFC-CLC cogeneration system based on CO2 separation with natural cooling

被引:0
|
作者
Zhang, Hongsheng [1 ]
Li, Hanlin [1 ]
Yang, Xiaoyu [2 ]
Zhang, Yipeng [1 ]
Liu, Yifeng [1 ]
Duan, Chenghong [1 ]
Qin, Jiyun [3 ]
机构
[1] Beijing Univ Chem Technol, Coll Mech & Elect Engn, Beijing 100029, Peoples R China
[2] China Natl Oil & Gas Explorat & Dev Co Ltd, Beijing 100034, Peoples R China
[3] Shanghai Maritime Univ, China Inst FTZ Supply Chain, Shanghai 201306, Peoples R China
关键词
Chemical looping combustion; Cogeneration; Solid oxide fuel cell; Thermodynamic analysis; Economic analysis; OXIDE FUEL-CELL; LOOPING HYDROGEN GENERATION; TECH-ECONOMIC ASSESSMENT; PERFORMANCE ANALYSIS; POWER PRODUCTION; CCHP SYSTEM; CYCLE; OPTIMIZATION; ENERGY; CAPTURE;
D O I
10.1016/j.enconman.2024.119172
中图分类号
O414.1 [热力学];
学科分类号
摘要
An advanced cogeneration system combining CLC (Chemical Looping Combustion) and SOFC (Solid Oxide Fuel Cell) is proposed to reduce CO2 separation energy consumption in this paper. The method can separate CO2 without energy consumption to achieve minimum carbon dioxide emissions through natural cooling and improve energy conversion efficiency. SOFC is used to efficiently transform chemical energy of fuel into electrical energy, and the CO2 separation is achieved without energy consumption by CLC technology to significantly reduce CO2 emission during the energy conversion process. Besides, absorption heat pump is utilized for the recovery of lowgrade cold-end waste heat to achieve dual goals of minimum CO2 emissions and zero waste heat emissions. The performances are evaluated from an energy, economic and exergy perspective. The study demonstrates that the efficiencies of power generation, exergy and thermal are 66.22 %, 74.01 % and 91.04 % under the design parameters. Compared to the reference system, the efficiencies of power generation, exergy and thermal are enhanced by 3.05 %, 4.36 %, and 3.53 %. The three components with the highest exergy losses are the SOFC, CLC and direct current-accommodation converter (DC-AC), and accounts for 28.07 %, 27.16 % and 17.63 %. The levelized cost of exergy (LCOE) is 0.1026 $/kWh. The dynamic payback period is 7.03 years, which is reduced by 2.35 years compared to the reference system. Additionally, a sensitivity analysis is conducted. As fuel utilization rate, SOFC operating pressure and SOFC operating temperature increase, the thermal efficiency remains around 91 %, and exergy efficiency rises from 68.26 %, 61.84 % and 69.57 % to 74.00 %, 73.51 % and 73.01 %, and power generation efficiency improves from 60.18 %, 54.62 % and 62.76 % to 66.22 %, 66.89 % and 66.48 %, while the heating load decreases from 75.88 kW, 88.80 kW and 69.38 kW to 61.40 kW, 59.67 kW and 61.09 kW. With an increase in current density, exergy efficiency and power generation efficiency decrease from 73.34 % and 66.71 % to 71.84 % and 65.14 %, and the heating load increases from 60.42 kW to 63.65 kW. As the split ratio increases, the thermal efficiency, exergy efficiency and heating load increase from 77.77 %, 72.57 % and 25 kW to 91.04 %, 72.88 % and 61.40 kW, while the power generation efficiency decreases from 67.66 % to 66.22 %.
引用
收藏
页数:19
相关论文
共 50 条
  • [21] Process and economic data for the thermo-economic analyses of IGCC power plants employing warm gas CO2 separation technology
    Rosner, Fabian
    Chen, Qin
    Rao, Ashok
    Samuelsen, Scott
    Jayaraman, Ambal
    Alptekin, Gokhan
    DATA IN BRIEF, 2019, 27
  • [22] Experimental study and thermo-economic analysis of a novel radiant-convective cooling system
    Jiang, Tingting
    You, Shijun
    Zhang, Huan
    Wei, Shen
    Liu, Huanzhi
    Wang, Yaran
    INTERNATIONAL JOURNAL OF REFRIGERATION, 2021, 131 (131) : 505 - 514
  • [23] Thermo-economic analysis and multi-objective optimization of cryogenic CO2 capture systems based on liquefied natural gas cold energy utilization
    Shu, Gequn
    Liu, Borui
    Tian, Hua
    Li, Ligeng
    Sun, Rui
    Wang, Xuan
    JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2024, 12 (05):
  • [24] Thermo-economic analysis of trigeneration system based on AA-CAES
    Han Z.
    Sun Y.
    Li P.
    Hu Q.
    Taiyangneng Xuebao/Acta Energiae Solaris Sinica, 2022, 43 (02): : 97 - 103
  • [25] Bio-gasification based Externally Fired Combined Cogeneration Plant: Thermo-economic Performance Analysis
    Mondal, P.
    Ghosh, S.
    MATERIALS TODAY-PROCEEDINGS, 2018, 5 (11) : 22963 - 22978
  • [26] Multi-objective optimization and thermo-economic analysis of an enhanced compression-absorption cascade refrigeration system and ORC integrated system for cooling and power cogeneration
    Sun, Xiaojing
    Liu, Linlin
    Dong, Yachao
    Zhuang, Yu
    Li, Jiao
    Du, Jian
    Yin, HongChao
    ENERGY CONVERSION AND MANAGEMENT, 2021, 236
  • [27] Thermo-economic analysis of regenerative supercritical CO2 Brayton cycle considering turbomachinery leakage flow
    Feng, Jiaqi
    Wang, Junpeng
    Chen, Zhentao
    Luo, Zhengyuan
    Bai, Bofeng
    ENERGY, 2024, 290
  • [28] THERMO-ECONOMIC ANALYSIS OF AN INTEGRATED SUPERCRITICAL CO2 BRAYTON CYCLE AND MULTIPLE EFFECT DESALINATION SYSTEMS
    Alharbi, Sattam
    Elsayed, Mohamed L.
    Chow, Louis
    PROCEEDINGS OF THE ASME INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION, 2018, VOL 6B, 2019,
  • [29] Thermo-economic optimization and part-load analysis of the combined supercritical CO2 and Kalina cycle
    Fan, Gang
    Dai, Yiping
    ENERGY CONVERSION AND MANAGEMENT, 2021, 245
  • [30] Analysis of Integration of MEA-Based CO2 Capture and Solar Energy System for Coal-Based Power Plants Based on Thermo-Economic Structural Theory
    Zhai, Rongrong
    Liu, Hongtao
    Wu, Hao
    Yu, Hai
    Yang, Yongping
    ENERGIES, 2018, 11 (05)