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dc.contributor.authorKwak, Rhokyun
dc.contributor.authorKwon, Hyukjin J.
dc.contributor.authorAl-Anzi, Bader
dc.contributor.authorLim, Geunbae
dc.contributor.authorKim, Bumjoo
dc.contributor.authorPham, Van-Sang
dc.contributor.authorKim, Minseok
dc.contributor.authorHan, Jongyoon
dc.date.accessioned2017-04-12T19:40:37Z
dc.date.available2017-04-12T19:40:37Z
dc.date.issued2016-08
dc.date.submitted2016-01
dc.identifier.issn2045-2322
dc.identifier.urihttp://hdl.handle.net/1721.1/108083
dc.description.abstractThere is an increasing need for the desalination of high concentration brine (>TDS 35,000 ppm) efficiently and economically, either for the treatment of produced water from shale gas/oil development, or minimizing the environmental impact of brine from existing desalination plants. Yet, reverse osmosis (RO), which is the most widely used for desalination currently, is not practical for brine desalination. This paper demonstrates technical and economic feasibility of ICP (Ion Concentration Polarization) electrical desalination for the high saline water treatment, by adopting multi-stage operation with better energy efficiency. Optimized multi-staging configurations, dependent on the brine salinity values, can be designed based on experimental and numerical analysis. Such an optimization aims at achieving not just the energy efficiency but also (membrane) area efficiency, lowering the true cost of brine treatment. ICP electrical desalination is shown here to treat brine salinity up to 100,000 ppm of Total Dissolved Solids (TDS) with flexible salt rejection rate up to 70% which is promising in a various application treating brine waste. We also demonstrate that ICP desalination has advantage of removing both salts and diverse suspended solids simultaneously, and less susceptibility to membrane fouling/scaling, which is a significant challenge in the membrane processes.en_US
dc.language.isoen_US
dc.publisherNature Publishing Groupen_US
dc.relation.isversionofhttp://dx.doi.org/10.1038/srep31850en_US
dc.rightsCreative Commons Attribution 4.0 International Licenseen_US
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/en_US
dc.sourceNatureen_US
dc.titlePurification of High Salinity Brine by Multi-Stage Ion Concentration Polarization Desalinationen_US
dc.typeArticleen_US
dc.identifier.citationKim, Bumjoo; Kwak, Rhokyun; Kwon, Hyukjin J.; Pham, Van Sang; Kim, Minseok; Al-Anzi, Bader; Lim, Geunbae and Han, Jongyoon. “Purification of High Salinity Brine by Multi-Stage Ion Concentration Polarization Desalination.” Scientific Reports 6 (August 22, 2016): 31850. © Authors 2016en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Electrical Engineering and Computer Scienceen_US
dc.contributor.departmentMassachusetts Institute of Technology. Research Laboratory of Electronicsen_US
dc.contributor.mitauthorKim, Bumjoo
dc.contributor.mitauthorPham, Van-Sang
dc.contributor.mitauthorKim, Minseok
dc.contributor.mitauthorHan, Jongyoon
dc.relation.journalScientific Reportsen_US
dc.eprint.versionFinal published versionen_US
dc.type.urihttp://purl.org/eprint/type/JournalArticleen_US
eprint.statushttp://purl.org/eprint/status/PeerRevieweden_US
dspace.orderedauthorsKim, Bumjoo; Kwak, Rhokyun; Kwon, Hyukjin J.; Pham, Van Sang; Kim, Minseok; Al-Anzi, Bader; Lim, Geunbae; Han, Jongyoonen_US
dspace.embargo.termsNen_US
dc.identifier.orcidhttps://orcid.org/0000-0003-2955-793X
dc.identifier.orcidhttps://orcid.org/0000-0001-7215-1439
mit.licensePUBLISHER_CCen_US


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