Heat Integration and Optimization of Supercritical CO2 Recompression Cycle Coupled with Oxy-Coal Combustion

被引:5
|
作者
Wang, Shun-sen [1 ]
Feng, Xue-jia [2 ]
Wu, Chuang [2 ]
机构
[1] Xi An Jiao Tong Univ, Inst Turbomachinery, State Key Lab Multiphase Flow Power Engn, Xian 710049, Shaanxi, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Xian 710049, Shaanxi, Peoples R China
关键词
Oxy-combustion; Supercritical CO2 cycle; Exergetic analysis; Thermodynamic optimization; FIRED POWER-PLANT; CARBON-DIOXIDE; PRE-COMBUSTION; CAPTURE; ENERGY; POSTCOMBUSTION; AMMONIA; TURBINE; EXERGY; SOFC;
D O I
10.1061/(ASCE)EY.1943-7897.0000581
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This study proposes a supercritical CO2 recompression cycle based on external oxy-coal combustion. It aims to evaluate and improve the performance of the system guided by energetic and exergetic analyses. The influence of the heat integration of the air separation unit (ASU) on performance is initially assessed and sensitivity analyses of cycle variables are then conducted. The system parameters are thermodynamically optimized using a genetic algorithm. Results show that the net efficiency of the base case is 42.13%. If ASU heat integration is considered, then the net efficiency increases to 45.1%, showing an efficiency increment of 2.97%. The comparison of the layouts reveals that the intercooled reheat cycle has the maximum net efficiency that can reach 47.73% when the optimal inlet and outlet pressures are 40 and 7.6 MPa, respectively. Finally, the proposed optimized system is compared with an ultra-supercritical pulverized coal (USC-PC) plant, and the economic performance is evaluated. Results show that the proposed optimized system is economically suitable, the net efficiency is comparable to that of the USC-PC plant, and the net efficiency with carbon capture is 4.27% higher than that of the USC-PC plant. (C) 2018 American Society of Civil Engineers.
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页数:18
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