Simulation and exergetic evaluation of CO2 capture in a solid-oxide fuel-cell combined-cycle power plant

被引:33
作者
Petrakopoulou, Fontina [1 ,2 ]
Lee, Young Duk [3 ,4 ]
Tsatsaronis, George [3 ]
机构
[1] Natl Tech Univ Athens, GR-15773 Athens, Greece
[2] Tech Univ Crete, Khania 73100, Greece
[3] Tech Univ Berlin, D-10587 Berlin, Germany
[4] Korea Inst Machinery & Mat, Taejon 305343, South Korea
关键词
SOFC; Fuel cell; CO2; capture; Exergetic analysis; Combined-cycle power plant; GAS-TURBINE; SOFC; GENERATION; TEMPERATURE; PERFORMANCE; COMBUSTION; SYSTEM;
D O I
10.1016/j.apenergy.2013.09.034
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
The incorporation of fuel cells into power plants can enhance the operational efficiency and facilitate the separation and capture of emissions. In this paper a fuel-cell unit, consisting of solid-oxide fuel-cell stacks, a pre-reformer, and an afterburner is incorporated into a combined-cycle power plant with CO2 capture. The thermodynamic performance of the plant is examined using an exergetic analysis and it is compared with a conventional combined-cycle power plant (reference plant) without CO2 capture, as well as with other plants with CO2 capture. The inefficiencies of the chemical reactions taking place in the fuel-cell unit are found to be the main source of exergy destruction among the plant components. However, the additional power generated in the fuel-cell stacks and the afterburner enhances the overall efficiency and compensates for the energy needed for the capture and compression of the carbon dioxide. When compared with the reference plant and with alternative capture technologies, the solid-oxide fuel-cell plant with CO2 capture operates more efficiently and appears to be a thermodynamically promising approach for carbon capture. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:417 / 425
页数:9
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