Simultaneous carbon dioxide capture and utilization using thermal desalination reject brine

Simultaneous carbon dioxide capture and utilization using thermal desalination reject brine •The simultaneous capture and utilization of CO2 with reject brine is feasible.•The use of 2 amino 2 methyl propanol (AMP) resulted in high precipitation yield.•The proposed amine process is a good replacement for ammonia in the Solvay process.•Higher brine concentration improved the CO2 absorption capacity. http://www.deepdyve.com/assets/images/DeepDyve-Logo-lg.png Applied Energy Elsevier

Simultaneous carbon dioxide capture and utilization using thermal desalination reject brine

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Publisher
Elsevier
Copyright
Copyright © 2015 Elsevier Ltd
ISSN
0306-2619
D.O.I.
10.1016/j.apenergy.2015.05.010
Publisher site
See Article on Publisher Site

Abstract

•The simultaneous capture and utilization of CO2 with reject brine is feasible.•The use of 2 amino 2 methyl propanol (AMP) resulted in high precipitation yield.•The proposed amine process is a good replacement for ammonia in the Solvay process.•Higher brine concentration improved the CO2 absorption capacity.

Journal

Applied EnergyElsevier

Published: Sep 15, 2015

References

  • CO2 utilisation
    Gale, J.
  • Techno-economic assessment and environmental impacts of desalination
    Toufic, M.; Hassan, F.; Zeina, A.; Arslan, K.
  • Reject brine management
    El Naas, M.
  • Dual purpose chemical desalination process
    Abdel Aal, H.K.; Ibrahim, A.A.; Shalabi, M.A.; Al Harbi, D.K.
  • Solubility of carbon dioxide in aqueous solution of monoethanolamine or 2-amino-2-methyl-1-propanol: experimental measurements and modelling
    Danlu, T.; Martin Trusler, J.P.; Geoffrey, C.M.; Jon, G.; Paul, S.F.

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