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Techno-Economic Assessment of Different Heat Exchangers for CO 2 Capture

Author

Listed:
  • Solomon Aforkoghene Aromada

    (Department of Process, Energy and Environmental Technology, University of South-Eastern Norway, Kjølnes Ring 56, 3918 Porsgrunn, Norway)

  • Nils Henrik Eldrup

    (Department of Process, Energy and Environmental Technology, University of South-Eastern Norway, Kjølnes Ring 56, 3918 Porsgrunn, Norway
    SINTEF Tel-Tek, SINTEF Industri, Kjølnes Ring 30, 3918 Porsgrunn, Norway)

  • Fredrik Normann

    (Department of Energy and Environment, Chalmers University of Technology, SE-412 96 Göteborg, Sweden)

  • Lars Erik Øi

    (Department of Process, Energy and Environmental Technology, University of South-Eastern Norway, Kjølnes Ring 56, 3918 Porsgrunn, Norway)

Abstract
We examined the cost implications of selecting six different types of heat exchangers as the lean/rich heat exchanger in an amine-based CO 2 capture process. The difference in total capital cost between different capture plant scenarios due to the different costs of the heat exchangers used as the lean/rich heat exchanger, in each case, is in millions of Euros. The gasketed-plate heat exchanger (G-PHE) saves significant space, and it saves considerable costs. Selecting the G-PHE instead of the shell and tube heat exchangers (STHXs) will save €33 million–€39 million in total capital cost (CAPEX), depending on the type of STHX. About €43 million and €2 million in total installed costs (CAPEX) can be saved if the G-PHE is selected instead of the finned double-pipe heat exchanger (FDP-HX) or welded-plate heat exchanger, respectively. The savings in total annual cost is also in millions of Euros/year. Capture costs of €5/tCO 2 –€6/tCO 2 can be saved by replacing conventional STHXs with the G-PHE, and over €6/tCO 2 in the case of the FDP-HX. This is significant, and it indicates the importance of clearly stating the exact type and not just the broad classification of heat exchanger used as lean/rich heat exchanger. This is required for cost estimates to be as accurate as possible and allow for appropriate comparisons with other studies. Therefore, the gasketed-plate heat exchanger is recommended to save substantial costs. The CO 2 capture costs of all scenarios are most sensitive to the steam cost. The plate and frame heat exchangers (PHEs) scenario’s capture cost can decline from about €77/tCO 2 to €59/tCO 2 or rise to €95/tCO 2 .

Suggested Citation

  • Solomon Aforkoghene Aromada & Nils Henrik Eldrup & Fredrik Normann & Lars Erik Øi, 2020. "Techno-Economic Assessment of Different Heat Exchangers for CO 2 Capture," Energies, MDPI, vol. 13(23), pages 1-27, November.
    • Handle: RePEc:gam:jeners:v:13:y:2020:i:23:p:6315-:d:453735
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    References listed on IDEAS

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    1. Solomon Aforkoghene Aromada & Bjørn Kvamme & Na Wei & Navid Saeidi, 2019. "Enthalpies of Hydrate Formation and Dissociation from Residual Thermodynamics," Energies, MDPI, vol. 12(24), pages 1-26, December.
    2. Li, Kangkang & Leigh, Wardhaugh & Feron, Paul & Yu, Hai & Tade, Moses, 2016. "Systematic study of aqueous monoethanolamine (MEA)-based CO2 capture process: Techno-economic assessment of the MEA process and its improvements," Applied Energy, Elsevier, vol. 165(C), pages 648-659.
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    Cited by:

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    3. Ma, Chunyan & Wang, Nan & Ye, Nannan & Ji, Xiaoyan, 2021. "CO2 capture using ionic liquid-based hybrid solvents from experiment to process evaluation," Applied Energy, Elsevier, vol. 304(C).

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