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- W2023366001 abstract "We present a model of a coal-fired power plant integrated with a dynamic model of a monoethanolamine (MEA)-based post-combustion CO2 capture process. We evaluate base- and part-load operating modes of the integrated power and CO2 capture plant. We propose a simple modification to the base-process which exploits the tradeoff between thermodynamic and rate or kinetic driving forces for mass transfer. This modification returns a portion of the regenerated solvent to the middle of the absorption column at an elevated temperature. Under base-load operation of the power plant, this modification was observed to increase the degree of CO2 capture by 9.9% and reduce the reboiler duty by 8.3%, improving the net electrical efficiency of the decarbonised power plant from 28.27% to 29.15% – a relative increase of 2.8%. Under part-load operation, the degree of CO2 capture increased by 1% with a concurrent reduction in reboiler duty of 16.7% and an increase in overall process efficiency of 3.25%." @default.
- W2023366001 created "2016-06-24" @default.
- W2023366001 creator A5002701966 @default.
- W2023366001 creator A5089095524 @default.
- W2023366001 date "2014-08-01" @default.
- W2023366001 modified "2023-09-25" @default.
- W2023366001 title "Dynamic modelling and analysis of a coal-fired power plant integrated with a novel split-flow configuration post-combustion CO2 capture process" @default.
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- W2023366001 doi "https://doi.org/10.1016/j.ijggc.2014.05.007" @default.
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