Comprehensive investigation of process characteristics for oxy-steam combustion power plants

被引:58
作者
Jin, Bo [1 ]
Zhao, Haibo [1 ]
Zou, Chun [1 ]
Zheng, Chuguang [1 ]
机构
[1] Huazhong Univ Sci & Technol, State Key Lab Coal Combust, Wuhan 430074, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
Oxy-steam combustion; Process simulation; Exergy analysis; Techno-economic evaluation; Solar energy; PULVERIZED-COAL; FUEL COMBUSTION; CHEMICAL MECHANISM; EXERGY ANALYSIS; CO2; OPTIMIZATION; TEMPERATURE; TECHNOLOGY; IGNITION;
D O I
10.1016/j.enconman.2015.04.031
中图分类号
O414.1 [热力学];
学科分类号
070201 [理论物理];
摘要
Oxy-steam combustion, as an alternative option of oxy-fuel combustion technology, is considered as a promising CO2 capture technology for restraining CO2 emissions from power plants. To attain its comprehensive process characteristics, process simulation, thermodynamic assessment, and sensitivity analysis for oxy-steam combustion pulverized-coal-fired power plants are investigated whilst its corresponding CO2/O-2 recycled combustion (oxy-CO2 combustion) power plant is served as the base case for comparison. Techno-economic evaluation and integration with solar parabolic trough collectors are also discussed to justify its economic feasibility and improve its thermodynamic performance further, respectively. It is found that oxy-steam combustion exhibits better performance than oxy-CO2 combustion on both thermodynamic and economic aspects, in which the cost of electricity decreases about 6.62% whilst the net efficiency and exergy efficiency increase about 0.90 and 1.01 percentage points, respectively. The increment of oxygen concentration in oxidant (20-45 mol.%) and decrease of excess oxygen coefficient (1.01-1.09) in a certain range are favorable for improving oxy-steam combustion system performance. Moreover, its thermodynamic performance can be improved when considering solar parabolic trough collectors for heating recycled water, even though its cost of electricity increases about 2 $/(MW h). (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:92 / 101
页数:10
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