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- W2972238809 abstract "This study evaluates a chain of units that consist of a supercritical steam power plant, CO2 capture unit, and CO2 liquefaction unit, in terms of energy production and usage. The steam power plant is fueled by Illinois no. 6 bituminous coal and designed to deliver a gross electrical power of 600 MW. Energy performance of two different solvents (30% wt. Monoethanolamine and 40% wt. Piperazine) were considered for CO2 capture unit, and a sensitivity analysis was done to ascertain the effect of Lean/Rich heat exchanger minimum temperature approach on energy consumption of the reboiler. Two separate liquid states of CO2 (19.7 bar, −20 °C and 26.5 bar, −10 °C), which their ship-based transportation feasibility was studied by Global Carbon Capture and Storage Institute, was considered as the state of produced CO2 stream. Three conventional and one novel liquefaction processes were evaluated to deliver CO2 stream at aforementioned liquid states. While both of simulated CO2 capture units are thermally integrated with the steam power plant, just the novel case of liquefaction process is integrated with the steam power plant. According to the results, the reboiler in 40% wt. Piperazine case was ascertained to have 11% less energy consumption than that of 30% wt. Monoethanolamine case. The novel liquefaction process shows the best energy performance, and its equivalent sacrificed electrical energy is the lowest among all. Comparison of all possible chains of cases in this study (19 possibilities) gives a deep insight about affecting parameters of carbon capture and liquefaction in post-combustion." @default.
- W2972238809 created "2019-09-12" @default.
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- W2972238809 date "2019-11-01" @default.
- W2972238809 modified "2023-09-29" @default.
- W2972238809 title "Energy assessment of coal-fired steam power plant, carbon capture, and carbon liquefaction process chain as a whole" @default.
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- W2972238809 doi "https://doi.org/10.1016/j.enconman.2019.111994" @default.
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