Journal
PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART E-JOURNAL OF PROCESS MECHANICAL ENGINEERING
Volume 227, Issue 3, Pages 149-156Publisher
SAGE PUBLICATIONS LTD
DOI: 10.1177/0954408912445855
Keywords
CO2 capture; chemical absorption; flue gas; energy penalty; power plant
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Funding
- Power Generation & Electricity Delivery of the Korea Institute of Energy Technology Evaluation and Planning (KETEP)
- Ministry of Knowledge Economy, Republic of Korea [2010201020006A]
- Korea Evaluation Institute of Industrial Technology (KEIT) [2010201020006A] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)
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In this study, a performance analysis of a 500MWe coal-fired power plant with a post-combustion CO2 capture system was performed. The amine-based chemical absorption process was considered as a base CO2 capture system. Based on the design conditions of the flue gas from the supercritical coal-fired power plant operating in the Republic of Korea, the energy consumption of the CO2 capture system was simulated using a process simulator. The simulation of the CO2 capture system was undertaken using Aspen Plus software with ELECNRTL property packages; based on these results, the energy requirement of the CO2 capture system and the overall efficiency of a power plant with the CO2 capture system was estimated. It was observed that the thermal energy required to regenerate the solvent reduces the efficiency of the power plant by 8.36%, the energy required to compress the CO2 from 0.1 to 11MPa is the next largest factor, reducing the efficiency by 3.59%, and the other energy requirement amounts to 0.45%.
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