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dc.contributor.author부찬희-
dc.contributor.authorRobert K. Winton-
dc.contributor.authorKelly M. Conway-
dc.contributor.authorNgai Yin Yip-
dc.date.accessioned2021-06-09T04:26:03Z-
dc.date.available2021-06-09T04:26:03Z-
dc.date.issued2019-06-
dc.identifier.citationVOL 6, NO 6-364-
dc.identifier.issn2328-8930-
dc.identifier.other56464-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/72793-
dc.description.abstractHypersaline brines are of growing environmental importance but are technologically under-served by today’s desalination methods. Temperature swing solvent extraction (TSSE) is a radically different desalination technology that is membrane-less and not based on evaporative phase change. TSSE utilizes low-temperature heat and a low-polarity solvent with temperature-dependent water solubility for the selective extraction of water over salt from saline feeds. This study demonstrates TSSE desalination of high-salinity brines simulated by NaCl solutions with three amine solvents: diisopropylamine (DIPA), N-ethylcyclohexylamine (ECHA), and N,N-dimethylcyclohexylamine (DMCHA). We show that TSSE can desalinate brines with salinities as high as ?234000 ppm total dissolved solids (i.e., 4.0 M NaCl) and achieve salt removals up to 98.4%. Among the solvents, DIPA exhibited the highest water extraction efficiency whereas ECHA and DMCHA produced water with the lowest salt content and solvent residue content, respectively. Lastly, a high water recovery of >50% was demonstrated for TSSE desalination of 1.5 M NaCl brine using DIPA in semibatch experiments with multiple extraction cycles. This study underscores the unique capabilities of TSSE for the desalination of hypersaline brines.-
dc.publisherEnvironmental Science and Technology Letters-
dc.titleMembrane-less and Non-Evaporative Desalination of Hypersaline Brines by Temperature Swing Solvent Extraction-
dc.typeArticle-
dc.relation.page359364-
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