Membrane-less and Non-Evaporative Desalination of Hypersaline Brines by Temperature Swing Solvent Extraction

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dc.contributor.authorBoo, Chanheeko
dc.contributor.authorWinton, Robert K.ko
dc.contributor.authorConway, Kelly M.ko
dc.contributor.authorYip, Ngai Yinko
dc.date.accessioned2023-08-03T07:00:52Z-
dc.date.available2023-08-03T07:00:52Z-
dc.date.created2023-08-03-
dc.date.created2023-08-03-
dc.date.issued2019-06-
dc.identifier.citationENVIRONMENTAL SCIENCE & TECHNOLOGY LETTERS, v.6, no.6, pp.359 - 364-
dc.identifier.issn2328-8930-
dc.identifier.urihttp://hdl.handle.net/10203/311085-
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 approximate to 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.languageEnglish-
dc.publisherAMER CHEMICAL SOC-
dc.titleMembrane-less and Non-Evaporative Desalination of Hypersaline Brines by Temperature Swing Solvent Extraction-
dc.typeArticle-
dc.identifier.wosid000471728900008-
dc.identifier.scopusid2-s2.0-85065863385-
dc.type.rimsART-
dc.citation.volume6-
dc.citation.issue6-
dc.citation.beginningpage359-
dc.citation.endingpage364-
dc.citation.publicationnameENVIRONMENTAL SCIENCE & TECHNOLOGY LETTERS-
dc.identifier.doi10.1021/acs.estlett.9b00182-
dc.contributor.localauthorBoo, Chanhee-
dc.contributor.nonIdAuthorWinton, Robert K.-
dc.contributor.nonIdAuthorConway, Kelly M.-
dc.contributor.nonIdAuthorYip, Ngai Yin-
dc.description.isOpenAccessN-
dc.type.journalArticleArticle-
dc.subject.keywordPlusREVERSE-OSMOSIS-
dc.subject.keywordPlusENERGY EFFICIENCY-
dc.subject.keywordPlusSHALE GAS-
dc.subject.keywordPlusWATER-
dc.subject.keywordPlusTECHNOLOGIES-
dc.subject.keywordPlusMANAGEMENT-
dc.subject.keywordPlusFUTURE-
dc.subject.keywordPlusDISTILLATION-
dc.subject.keywordPlusCHALLENGES-
dc.subject.keywordPlusDRIVERS-
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