DC Field | Value | Language |
---|---|---|
dc.contributor.author | Boo, Chanhee | ko |
dc.contributor.author | Winton, Robert K. | ko |
dc.contributor.author | Conway, Kelly M. | ko |
dc.contributor.author | Yip, Ngai Yin | ko |
dc.date.accessioned | 2023-08-03T07:00:52Z | - |
dc.date.available | 2023-08-03T07:00:52Z | - |
dc.date.created | 2023-08-03 | - |
dc.date.created | 2023-08-03 | - |
dc.date.issued | 2019-06 | - |
dc.identifier.citation | ENVIRONMENTAL SCIENCE & TECHNOLOGY LETTERS, v.6, no.6, pp.359 - 364 | - |
dc.identifier.issn | 2328-8930 | - |
dc.identifier.uri | http://hdl.handle.net/10203/311085 | - |
dc.description.abstract | Hypersaline 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.language | English | - |
dc.publisher | AMER CHEMICAL SOC | - |
dc.title | Membrane-less and Non-Evaporative Desalination of Hypersaline Brines by Temperature Swing Solvent Extraction | - |
dc.type | Article | - |
dc.identifier.wosid | 000471728900008 | - |
dc.identifier.scopusid | 2-s2.0-85065863385 | - |
dc.type.rims | ART | - |
dc.citation.volume | 6 | - |
dc.citation.issue | 6 | - |
dc.citation.beginningpage | 359 | - |
dc.citation.endingpage | 364 | - |
dc.citation.publicationname | ENVIRONMENTAL SCIENCE & TECHNOLOGY LETTERS | - |
dc.identifier.doi | 10.1021/acs.estlett.9b00182 | - |
dc.contributor.localauthor | Boo, Chanhee | - |
dc.contributor.nonIdAuthor | Winton, Robert K. | - |
dc.contributor.nonIdAuthor | Conway, Kelly M. | - |
dc.contributor.nonIdAuthor | Yip, Ngai Yin | - |
dc.description.isOpenAccess | N | - |
dc.type.journalArticle | Article | - |
dc.subject.keywordPlus | REVERSE-OSMOSIS | - |
dc.subject.keywordPlus | ENERGY EFFICIENCY | - |
dc.subject.keywordPlus | SHALE GAS | - |
dc.subject.keywordPlus | WATER | - |
dc.subject.keywordPlus | TECHNOLOGIES | - |
dc.subject.keywordPlus | MANAGEMENT | - |
dc.subject.keywordPlus | FUTURE | - |
dc.subject.keywordPlus | DISTILLATION | - |
dc.subject.keywordPlus | CHALLENGES | - |
dc.subject.keywordPlus | DRIVERS | - |
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