Performance assessment and system optimization on supercritical CO2 double-path recompression coal-fired combined heat and power plants with MEA-based post-combustion CO2 capture

被引:17
作者
Zhou, Jing [1 ,2 ]
Zhu, Meng [1 ]
Chen, Lei [1 ]
Ren, Qiangqiang [1 ]
Su, Sheng [1 ]
Hu, Song [1 ]
Wang, Yi [1 ]
Xiang, Jun [1 ,3 ]
机构
[1] Huazhong Univ Sci & Technol, Sch Energy & Power Engn, State Key Lab Coal Combust, Wuhan 430074, Peoples R China
[2] Nanyang Technol Univ, Sch Comp Sci & Engn, Singapore 637141, Singapore
[3] 1037 Luoyu Rd, Wuhan 430074, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
Supercritical carbon dioxide cycle; Combined heat and power; Post -combustion carbon capture; Performance analysis and system optimization; CARBON-DIOXIDE; EXERGY ANALYSIS; PARAMETRIC ANALYSIS; BRAYTON CYCLES; MONOETHANOLAMINE; COGENERATION; COMBUSTION; TURBINE;
D O I
10.1016/j.energy.2022.126539
中图分类号
O414.1 [热力学];
学科分类号
摘要
Combined heat and power (CHP) is the technical means to realize the joint and efficient production of thermal and electrical energy. This study aims to construct the performance analysis and system optimization methods of supercritical CO2 (S-CO2) coal-fired CHP plants with MEA-based post-combustion carbon capture and storage (CCS) that has adapted for various S-CO2 CHP cycles. S-CO2 recompression CHP cycle has imperfect adaptability and exhibits significant optimization potential based on energy and exergy analysis, as it shows substantial advantages over the S-CO2 power cycle. And S-CO2 double-path compression (DPR) coal-fired CHP plants have been proposed to decouple the system heating and power generation. Results show that exergy efficiency of S-CO2 DPR coal-fired CHP units at 0% and 100% heating loads (HL) are 43.22% and 46.21%, increasing by 9.81% and 1.01% compared with S-CO2 recompression CHP units, respectively. What is more advantageous is that S-CO2 DPR coal-fired CHP plant has the lower exergy efficiency decline (8.43% and 8.37% at 0% and 100% HL) with MEA-based CCS, showing more refined energy cascade utilization with heating supply, electricity generation and carbon capture. Sensitivity analysis of cycle maximum temperature and ion absorption tech-nology is also performed, showing the excellent prospects of industrialization demonstration.
引用
收藏
页数:18
相关论文
共 44 条
[1]   Thermoeconomic performance and optimization of a novel cogeneration system using carbon dioxide as working fluid [J].
Akbari, A. D. ;
Mahmoudi, S. M. S. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 145 :265-277
[2]   Thermodynamic analysis of a novel integrated system operating with gas turbine, s-CO2 and t-CO2 power systems for hydrogen production and storage [J].
Altinkaynak, Mehmet ;
Ozturk, Murat .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2022, 47 (05) :3484-3503
[3]  
[Anonymous], 2004, ROYAL DECREE 436 200, P59
[4]  
[Anonymous], 2019, OUTLOOK BE
[5]   300 MW boiler design study for coal-fired supercritical C02 Brayton cycle [J].
Bai, Wengang ;
Zhang, Yifan ;
Yang, Yu ;
Li, Hongzhi ;
Yao, Mingyu .
APPLIED THERMAL ENGINEERING, 2018, 135 :66-73
[6]  
Blum Rudolph, 2009, VGB Powertech, V89, P26
[7]   Energy-saving mechanism and parametric analysis of the high back-pressure heating process in a 300 MW coal-fired combined heat and power unit [J].
Chen, Heng ;
Xiao, Yao ;
Xu, Gang ;
Xu, Jidong ;
Yao, Xianhuai ;
Yang, Yongping .
APPLIED THERMAL ENGINEERING, 2019, 149 :829-840
[8]  
Dale S., 2019, BP STAT REV WORLD EN, P14
[9]  
Dostal V., 2004, MIT-ANP-TR-100
[10]   Advanced exergy analysis of the combined S-CO2/ORC system [J].
Fallah, M. ;
Mohammadi, Z. ;
Mahmoudi, S. M. Seyed .
ENERGY, 2022, 241