4.7 Article

Performance prediction and evaluation of CO2 utilization with conjoined electrolysis and carbonation using desalinated rejected seawater brine

Journal

DESALINATION
Volume 509, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.desal.2021.115068

Keywords

Pollutant treatment; Desalinated rejected brine; Carbon capture utilization (CCU); Electrolysis; Process evaluation; Metal cation

Funding

  1. KOREA SOUTH-EAST POWER CO. [2020KOEN (Yeongdong) 02]
  2. Technology Innovation Program - Ministry of Trade, Industry and Energy (MOTIE, Korea) [20005884]
  3. Korea Evaluation Institute of Industrial Technology (KEIT) [20005884] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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The study proposes and evaluates the process of simultaneous treatment of oceanic and atmospheric pollutants based on simulation performance. Using desalinated rejected brine with high metal ion content and low cost allows for a stable source of feedstock and progress toward a sustainable electrolysis environment. Utilizing metal cations in desalinated wastewater can help overcome limitations in current technologies, particularly in carbon capture and utilization (CCU) technology.
The study of the simultaneous oceanic and atmospheric pollutant treatment process is proposed and evaluated based on the simulation performance. High contents of metal ions and low costs are some of the advantages in using desalinated rejected brine, which allows to have a stable feedstock source and to take some steps toward a sustainable electrolysis environment. By using metal cations present in desalinated wastewater, carbon capture and utilization (CCU) technology can overcome the limitations in present technologies. Mineral carbonation at ambient temperature using electrolysis has been designed. To evaluate the proposed process, a simulation compromising both electrolysis of brine and carbonation process is applied to estimate the energy consumption. As a result, about 91.3% of CO2 is captured from flue gas, and CaCO3 and MgCO3 are produced as final products. The simulation results reveal that operational cost is highly dependent on the electricity price, so different scenarios were consulted to assess the economic feasibility of the process. The proposed design was compared with alternative CCUS technology to comment on their limitations and viability of its application.

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