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Analysis of Combined Cycle Power Plants with Chemical Looping Reforming of Natural Gas and Pre-Combustion CO 2 Capture

Author

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  • Shareq Mohd Nazir

    (Department of Energy and Process Engineering, Norwegian University of Science and Technology, 7491 Trondheim, Norway)

  • Olav Bolland

    (Department of Energy and Process Engineering, Norwegian University of Science and Technology, 7491 Trondheim, Norway)

  • Shahriar Amini

    (Department of Energy and Process Engineering, Norwegian University of Science and Technology, 7491 Trondheim, Norway
    SINTEF Materials and Chemistry, 7034 Trondheim, Norway)

Abstract

In this paper, a gas-fired combined cycle power plant subjected to a pre-combustion CO 2 capture method has been analysed under different design conditions and different heat integration options. The power plant configuration includes the chemical looping reforming (CLR) of natural gas (NG), water gas shift (WGS) process, CO 2 capture and compression, and a hydrogen fuelled combined cycle to produce power. The process is denoted as a CLR-CC process. One of the main parameters that affects the performance of the process is the pressure for the CLR. The process is analysed at different design pressures for the CLR, i.e., 5, 10, 15, 18, 25 and 30 bar. It is observed that the net electrical efficiency increases with an increase in the design pressure in the CLR. Secondly, the type of steam generated from the cooling of process streams also effects the net electrical efficiency of the process. Out of the five different cases including the base case presented in this study, it is observed that the net electrical efficiency of CLR-CCs can be improved to 46.5% (lower heating value of NG basis) by producing high-pressure steam through heat recovery from the pre-combustion process streams and sending it to the Heat Recovery Steam Generator in the power plant.

Suggested Citation

  • Shareq Mohd Nazir & Olav Bolland & Shahriar Amini, 2018. "Analysis of Combined Cycle Power Plants with Chemical Looping Reforming of Natural Gas and Pre-Combustion CO 2 Capture," Energies, MDPI, vol. 11(1), pages 1-13, January.
    • Handle: RePEc:gam:jeners:v:11:y:2018:i:1:p:147-:d:125887
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    References listed on IDEAS

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    Cited by:

    1. Nazir, Shareq Mohd & Cloete, Jan Hendrik & Cloete, Schalk & Amini, Shahriar, 2019. "Gas switching reforming (GSR) for power generation with CO2 capture: Process efficiency improvement studies," Energy, Elsevier, vol. 167(C), pages 757-765.
    2. Kazemi, Abolghasem & Moreno, Jovita & Iribarren, Diego, 2022. "Techno-economic comparison of optimized natural gas combined cycle power plants with CO2 capture," Energy, Elsevier, vol. 255(C).
    3. Xiaotong Ma & Yingjie Li & Yi Qian & Zeyan Wang, 2019. "A Carbide Slag-Based, Ca 12 Al 14 O 33 -Stabilized Sorbent Prepared by the Hydrothermal Template Method Enabling Efficient CO 2 Capture," Energies, MDPI, vol. 12(13), pages 1-17, July.
    4. Esveidi Montserrat Valdovinos-García & Juan Barajas-Fernández & María de los Ángeles Olán-Acosta & Moisés Abraham Petriz-Prieto & Adriana Guzmán-López & Micael Gerardo Bravo-Sánchez, 2020. "Techno-Economic Study of CO 2 Capture of a Thermoelectric Plant Using Microalgae ( Chlorella vulgaris ) for Production of Feedstock for Bioenergy," Energies, MDPI, vol. 13(2), pages 1-19, January.
    5. Hachem Hamadeh & Sannan Y. Toor & Peter L. Douglas & S. Mani Sarathy & Robert W. Dibble & Eric Croiset, 2020. "Techno-Economic Analysis of Pressurized Oxy-Fuel Combustion of Petroleum Coke," Energies, MDPI, vol. 13(13), pages 1-12, July.

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