Techno-economic analysis of ion concentration polarization desalination for high salinity desalination applications
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CHOI-Tech_Water Research_Manuscript_Clean version.pdf
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Accepted version
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Author(s) • • • • • • • •
Al-Anzi, Bader
Choi, Siwon
Kim, Bumjoo
Nayar, Kishor Govind
Yoon, Junghyo
Al Hammadi, Yousef
Lienhard, John H
Han, Jongyoon
Al-Anzi, Bader
Date Issued
May 2019
Journal
Water Research
Publisher
Elsevier BV
Citation
Choi, Siwon et al. "Techno-economic analysis of ion concentration polarization desalination for high salinity desalination applications." Water Research 155 (May 2019): 162-174 © 2019 Elsevier Ltd
Version
Author's final manuscript
Abstract
A techno-economic analysis is used to evaluate the economic feasibility of ion concentration polarization (ICP) desalination for seawater desalination and brine management. An empirical optimization model based on a limited set of experimental data, which was obtained from a lab-scale ICP desalination prototype, was established to calculate the required energy and membrane area for a given set of operating parameters. By calculating operating and capital expenses in various feed and product cases, the optimal levelized cost of water is determined over a range of feed salinities, mostly above seawater salinity (35 g/kg). Through these analyses, we study the economic feasibility of three applications: 1) partial desalination of brine discharge by ICP (feed varied from 35 to 75 g/kg) to common seawater RO feed level (35 g/kg) in a hybrid ICP-RO system; 2) the concentration of seawater desalination brine for salt production, and 3) partial desalination of oilfield wastewater. The economic feasibility of ICP desalination processes has been evaluated and the rough cost of treatment has been generated for several relevant applications. The approach taken in this work could be employed for other new and existing desalination processes, where a priori process modeling and optimization is scientifically and/or numerically challenging. Keywords: Electromembrane desalination; High salinity desalination; Brine management; Economic analysis; Ion concentration polarization
MIT Department
Massachusetts Institute of Technology. Department of Chemical Engineering
Massachusetts Institute of Technology. Department of Electrical Engineering and Computer Science
Massachusetts Institute of Technology. Department of Mechanical Engineering
Massachusetts Institute of Technology. Department of Biological Engineering
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DOI of Published Version
https://doi.org/10.1016/j.watres.2019.02.023