Thermodynamic and Economic Analysis of Oxy-Fuel-Integrated Coal Partial Gasification Combined Cycle

被引:5
|
作者
Ye, Chao [1 ]
Ye, Zefu [2 ]
Zhu, Zhujun [2 ]
Wang, Qinhui [3 ]
机构
[1] Zhejiang Univ Sci & Technol, Dept Energy & Environm Syst Engn, Hangzhou 310023, Zhejiang, Peoples R China
[2] Shanxi Gemeng US China Clean Energy R&D Ctr Co Lt, Taiyuan 030000, Shanxi, Peoples R China
[3] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
来源
ACS OMEGA | 2021年 / 6卷 / 06期
关键词
FIRED POWER-PLANT; FLUIDIZED-BED; TECHNOECONOMIC ANALYSIS; CARBON CAPTURE; HIGH-TEMPERATURE; NATURAL-GAS; FLUE-GAS; COMBUSTION; BIOMASS; GENERATION;
D O I
10.1021/acsomega.0c05277
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A novel partial gasification combined cycle (PGCC ) system integrating coal partial gasification, oxy-fuel combustion, combined cycle, and CO2 separation is proposed. The coal-CO2 partial gasification technology is introduced in the coal gasification unit, and the oxy-fuel combustion technology is employed in the char combustion unit and gas turbine (GT) unit. The thermodynamic and economic analysis of the proposed system is carried out, showing that both energy and exergy efficiency have an increasing/decreasing tendency when the recycled flue gas (RFG) ratio of char combustion and GT increase. When the RFG ratios of char combustion and GT are 0.43 and 0.34, energy and exergy efficiencies reach maximum values of 48.18 and 45.11%, respectively. The energy efficiency of the PGCC-Oxy system is higher than that of the integrated gasification combined cycle (IGCC)-Oxy system by approximately 3%. It can be concluded from the economic analysis that the total investment on the PGCCOxy system is 3272.71 million RMB, and the internal rate of return (IRR) and payback time is 8.07% and 12.38 years, respectively.
引用
收藏
页码:4262 / 4272
页数:11
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