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Parametric Process Design and Economic Analysis of Post-Combustion CO 2 Capture and Compression for Coal- and Natural Gas-Fired Power Plants

Author

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  • Emmanuel Adu

    (Department of Oil and Gas Storage and Transportation Engineering, School of Petroleum Engineering, Yangtze University, Wuhan 430100, China
    Mechanical Engineering Department, Faculty of Engineering and Technology, Kumasi Technical University, P. O. Box 854 Kumasi, Ghana)

  • Y.D. Zhang

    (Department of Oil and Gas Storage and Transportation Engineering, School of Petroleum Engineering, Yangtze University, Wuhan 430100, China
    Measurement Science and Standards, National Research Council Canada, Building M-9, 1200 Montreal Road, Ottawa, ON K1A OR6, Canada)

  • Dehua Liu

    (Department of Oil and Gas Storage and Transportation Engineering, School of Petroleum Engineering, Yangtze University, Wuhan 430100, China)

  • Paitoon Tontiwachwuthikul

    (Clean Energy Technologies Research Institute (CETRI), Faculty of Engineering and Applied Science, University of Regina, 3737 Wascana Parkway, Regina, SK S4S0A2, Canada)

Abstract

For the envisaged large number of commercial-scale carbon capture and storage (CCS) projects that are to be implemented in the near future, a number of issues still need to be resolved, the most prominent being the large capital and operational costs incurred for the CO 2 capture and compression process. An economic assessment of the capture and compression system based on optimal design data is important for CCS deployment. In this paper, the parametric process design approach is used to optimally design coal and natural gas monoethanolamine (MEA)-based post-combustion CO 2 absorption–desorption capture (PCC) and compression plants that can be integrated into large-scale 550 MW coal-fired and 555 MW natural gas combined cycle (NGCC) power plants, respectively, for capturing CO 2 from their flue gases. The study then comparatively assesses the energy performance and economic viabilities of both plants to ascertain their operational feasibilities and relative costs. The parametric processes are presented and discussed. The results indicate that, at 90% CO 2 capture efficiency, for the coal PCC plant, with 13.5 mol.% CO 2 in the inlet flue gas, at an optimum liquid/gas ratio of 2.87 kg/kg and CO 2 lean loading of 0.2082 mol CO 2 /mol MEA, the CO 2 avoidance cost is about $72/tCO 2 , and, for the NGCC PCC plant, with 4.04 mol.% CO 2 in the inlet flue gas, at an optimum liquid/gas ratio of 0.98 kg/kg and CO 2 lean loading of 0.2307 mol CO 2 /mol MEA, the CO 2 avoidance cost is about $94/tCO 2 .

Suggested Citation

  • Emmanuel Adu & Y.D. Zhang & Dehua Liu & Paitoon Tontiwachwuthikul, 2020. "Parametric Process Design and Economic Analysis of Post-Combustion CO 2 Capture and Compression for Coal- and Natural Gas-Fired Power Plants," Energies, MDPI, vol. 13(10), pages 1-28, May.
    • Handle: RePEc:gam:jeners:v:13:y:2020:i:10:p:2519-:d:358854
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    References listed on IDEAS

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    1. Leung, Dennis Y.C. & Caramanna, Giorgio & Maroto-Valer, M. Mercedes, 2014. "An overview of current status of carbon dioxide capture and storage technologies," Renewable and Sustainable Energy Reviews, Elsevier, vol. 39(C), pages 426-443.
    2. Nataly Echevarria Huaman, Ruth & Xiu Jun, Tian, 2014. "Energy related CO2 emissions and the progress on CCS projects: A review," Renewable and Sustainable Energy Reviews, Elsevier, vol. 31(C), pages 368-385.
    3. McCollum, David L & Ogden, Joan M, 2006. "Techno-Economic Models for Carbon Dioxide Compression, Transport, and Storage & Correlations for Estimating Carbon Dioxide Density and Viscosity," Institute of Transportation Studies, Working Paper Series qt1zg00532, Institute of Transportation Studies, UC Davis.
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    Cited by:

    1. Josselyne A. Villarroel & Alex Palma-Cando & Alfredo Viloria & Marvin Ricaurte, 2021. "Kinetic and Thermodynamic Analysis of High-Pressure CO 2 Capture Using Ethylenediamine: Experimental Study and Modeling," Energies, MDPI, vol. 14(20), pages 1-15, October.
    2. Andrey Rogalev & Nikolay Rogalev & Vladimir Kindra & Ivan Komarov & Olga Zlyvko, 2021. "Research and Development of the Oxy-Fuel Combustion Power Cycles with CO 2 Recirculation," Energies, MDPI, vol. 14(10), pages 1-18, May.
    3. Branimir Tramošljika & Paolo Blecich & Igor Bonefačić & Vladimir Glažar, 2021. "Advanced Ultra-Supercritical Coal-Fired Power Plant with Post-Combustion Carbon Capture: Analysis of Electricity Penalty and CO 2 Emission Reduction," Sustainability, MDPI, vol. 13(2), pages 1-20, January.
    4. Julio, Alisson Aparecido Vitoriano & Castro-Amoedo, Rafael & Maréchal, François & González, Aldemar Martínez & Escobar Palacio, José Carlos, 2023. "Exergy and economic analysis of the trade-off for design of post-combustion CO2 capture plant by chemical absorption with MEA," Energy, Elsevier, vol. 280(C).

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