Integration of chemical looping combustion and supercritical CO2 cycle for combined heat and power generation with CO2 capture

被引:38
|
作者
Chen, Shiyi [1 ]
Soomro, Ahsanullah [1 ]
Yu, Ran [1 ]
Hu, Jun [1 ]
Sun, Zhao [1 ]
Xiang, Wenguo [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Minist Educ, Key Lab Energy Thermal Convers & Control, Nanjing 210096, Jiangsu, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
Chemical looping combustion; Supercritical CO2 cycle; CO2; capture; Combined heat and power; GASIFICATION COMBINED-CYCLE; ORGANIC RANKINE-CYCLE; FLUIDIZED-BED SYSTEM; OXYGEN CARRIER; BRAYTON CYCLES; CARBON CAPTURE; PERFORMANCE ANALYSIS; EXERGY ANALYSIS; REACTOR SYSTEM; GASEOUS FUELS;
D O I
10.1016/j.enconman.2018.04.083
中图分类号
O414.1 [热力学];
学科分类号
摘要
Chemical looping combustion (CLC) is an emerging technology for energy conversion with inherent CO2 separation. Supercritical CO2 (sCO(2)) Brayton cycle is a promising way for efficient power production with compactness. In this work, CLC and sCO(2) cycle were integrated for combined heat and power (CHP) cogeneration with CO2 capture. Coal was directly used as fuel for CLC, and CLC acted as heat source to drive a sCO(2) cycle with reheating and recompression. The heat in sCO(2) cooling and CO2 compression processes was recovered for district heating. A comprehensive analysis with first law based efficiency was performed to investigate the performance of the proposed cycle. For a baseline case of the proposed configuration, the net power efficiency was 41.3%, the heating efficiency was 40.4% and the resulting total efficiency was 81.7%, including CO2 compression to 120 bar. The effects of turbine inlet temperature, turbine inlet pressure, fuel reactor temperature, air reactor temperature, oxygen carrier ratio, inert support ratio, and air ratio on the thermal performance, including net power efficiency, heating efficiency, and total efficiency were analyzed as well.
引用
收藏
页码:113 / 124
页数:12
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