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Conceptualization of CO 2 Terminal for Offshore CCS Using System Engineering Process

Author

Listed:
  • Hyonjeong Noh

    (Offshore Industries R&BD Center, Korea Research Institute of Ships & Ocean Engineering, Geoje 53201, Korea)

  • Kwangu Kang

    (Offshore Industries R&BD Center, Korea Research Institute of Ships & Ocean Engineering, Geoje 53201, Korea)

  • Cheol Huh

    (Ocean Science & Technology School, Korea Maritime and Ocean University, Busan 49112, Korea)

  • Seong-Gil Kang

    (Global Cooperation Center, Korea Research Institute of Ships & Ocean Engineering, Daejeon 34103, Korea)

  • Seong Jong Han

    (Offshore Industries R&BD Center, Korea Research Institute of Ships & Ocean Engineering, Geoje 53201, Korea)

  • Hyungwoo Kim

    (Offshore Industries R&BD Center, Korea Research Institute of Ships & Ocean Engineering, Geoje 53201, Korea)

Abstract

In this study, the basic configuration and operation concept of a CO 2 terminal were identified by conducting a system engineering process. The performance goal of a CO 2 terminal was determined by requirement analysis. Then, functions and timelines were derived by functional analysis to meet the performance goal. Equipment to perform the functions were defined and finally, a process flow block diagram of the CO 2 terminal was acquired. The CO 2 terminal in this study consisted of three parts. First, the CO 2 loading/unloading part is responsible for liquid CO 2 unloading from the carrier and loading vapor CO 2 onto the carrier. Secondly, the liquid CO 2 transmission part extracts liquid CO 2 from the storage tanks and increases the pressure until it satisfies the offshore pipeline transportation condition. The vapor-treatment part collects boil-off gas, generates vapor CO 2 , and charges the storage tanks with vapor CO 2 to control the pressure of the storage tanks that discharge liquid CO 2 . Finally, the study results were compared with a liquefied natural gas (LNG) terminal. The biggest difference between the CO 2 terminal in this study and the LNG terminal is that a vaporizer is essential in the CO 2 terminal due to the smaller storage capacity of the CO 2 terminal and, therefore, the lower amount of boil-off gas.

Suggested Citation

  • Hyonjeong Noh & Kwangu Kang & Cheol Huh & Seong-Gil Kang & Seong Jong Han & Hyungwoo Kim, 2019. "Conceptualization of CO 2 Terminal for Offshore CCS Using System Engineering Process," Energies, MDPI, vol. 12(22), pages 1-18, November.
    • Handle: RePEc:gam:jeners:v:12:y:2019:i:22:p:4350-:d:287258
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    References listed on IDEAS

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    1. Kwangu Kang & Youngkyun Seo & Daejun Chang & Seong-Gil Kang & Cheol Huh, 2015. "Estimation of CO 2 Transport Costs in South Korea Using a Techno-Economic Model," Energies, MDPI, vol. 8(3), pages 1-21, March.
    2. Yoo, Byeong-Yong, 2017. "The development and comparison of CO2 BOG re-liquefaction processes for LNG fueled CO2 carriers," Energy, Elsevier, vol. 127(C), pages 186-197.
    3. Trotter, Ian M. & Gomes, Marília Fernandes Maciel & Braga, Marcelo José & Brochmann, Bjørn & Lie, Ole Nikolai, 2016. "Optimal LNG (liquefied natural gas) regasification scheduling for import terminals with storage," Energy, Elsevier, vol. 105(C), pages 80-88.
    4. Jung, Jung-Yeul & Huh, Cheol & Kang, Seong-Gil & Seo, Youngkyun & Chang, Daejun, 2013. "CO2 transport strategy and its cost estimation for the offshore CCS in Korea," Applied Energy, Elsevier, vol. 111(C), pages 1054-1060.
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    Cited by:

    1. Feng Chen & Tatiana Morosuk, 2021. "Exergetic and Economic Evaluation of CO 2 Liquefaction Processes," Energies, MDPI, vol. 14(21), pages 1-13, November.

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