Carbon dioxide capture in large-scale CCGT power plant from flue gases obtained from various fuel mixtures

被引:1
作者
Subramanian, Navaneethan [1 ]
Madejski, Pawel [1 ]
机构
[1] AGH Univ Sci & Technol, Fac Mech Engn & Robot, Al Mickiewicza 30, PL-30059 Krakow, Poland
关键词
Thermodynamic modelling; Combined Cycle Gas Turbine; Post-combustion carbon capture and storage; CO2; capture; Negative emission;
D O I
10.24425/ather.2024.151999
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this study, the thermodynamic analysis of a combined cycle gas turbine integrated with post-combustion carbon capture and storage using the solvent method is performed. The syngas obtained from the gasification of sewage sludge is mixed with methane and nitrogen-rich natural gas fuels at different proportions, used in the gas turbine, and the properties of fuel and flue gases are analyzed. The flue gas obtained from the fuel mixture is passed through the post-combustion carbon capture and storage at various load conditions to assess the heat and electricity required for the carbon capture process. The solvent used for the carbon capture from flue gases enables CO2 capture with the high efficiency of 90%. With the calculated results, the load conditions of flue gas using fuel mixtures are identified, which reduces the heat and power demand of post-combustion carbon capture and storage and provides the possibility to achieve neutral emission. The impact of selected operating conditions of post-combustion carbon capture and storage on the CO2 emission reduction process and on the power plant performances is investigated. Considering the factors of electricity generation, energy efficiency, heat supply to the consumers, operating load of post-combustion carbon capture and storage and CO2 emission, the 50% mixture of syngas with both fuels performs better. Also, the use of a mixture of 2-amino-2methyl-1-propanol and piperazine with reboiler duty 3.7 MJ/kgCO2 in post-combustion carbon capture and storage slightly enhanced the performance of the power plant compared to the use of monoethanolamine with reboiler duty 3.8 MJ/kgCO2.
引用
收藏
页码:85 / 93
页数:9
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