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Application of nanofiltration pretreatment to remove divalent ions for economical seawater reverse osmosis desalination

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dc.contributor.authorPark, Minho-
dc.contributor.authorPark, Jongkwan-
dc.contributor.authorLee, Eunkyung-
dc.contributor.authorKhim, Jeehyeong-
dc.contributor.authorCho, Jaeweon-
dc.date.accessioned2021-09-04T05:31:12Z-
dc.date.available2021-09-04T05:31:12Z-
dc.date.created2021-06-18-
dc.date.issued2016-
dc.identifier.issn1944-3994-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/90385-
dc.description.abstractTo minimize scale formation potential in the applications of reverse osmosis (RO) membranes as a pretreatment unit, relatively loose nanofiltration (NF) membrane systems coupled with ultrafiltration (UF) were used to remove divalent ions from seawater. However, the UF did not reject any ions because of pore size. The rejection of divalent ions by NF was in order of sulfate (>95%), magnesium (>60%), and calcium (>30%) in every rejection experiment based on water recovery rate (40, 50, 60, 70, and 80%). In the UF/NF/RO hybrid pilot system, most of the divalent (>99%) and the monovalent (>97%) ions were effectively rejected with slightly increased divalent ion rejection compared to the UF/RO system. Seawater temperature influenced rejection of ions with regards to either the diffusion- or convection-dominant transport of ions through the membrane pores. Electric power consumption was also compared between the UF/NF/RO process and the UF/RO process. For different salinity conditions (28,000 and 45,000mg/L of total dissolved solids), the lowest energy consumption by NF/RO was 3.3 and 6kWh/m(3) with recovery of 80% for NF and 40% for RO, respectively.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherTAYLOR & FRANCIS INC-
dc.subjectMEMBRANE-CHARACTERISTICS-
dc.subjectTRANSPORT PARAMETERS-
dc.subjectENERGY-CONSUMPTION-
dc.subjectTEMPERATURE-
dc.subjectPERFORMANCE-
dc.subjectOPERATIONS-
dc.titleApplication of nanofiltration pretreatment to remove divalent ions for economical seawater reverse osmosis desalination-
dc.typeArticle-
dc.contributor.affiliatedAuthorKhim, Jeehyeong-
dc.identifier.doi10.1080/19443994.2015.1111807-
dc.identifier.scopusid2-s2.0-84947727502-
dc.identifier.wosid000382975100005-
dc.identifier.bibliographicCitationDESALINATION AND WATER TREATMENT, v.57, no.44, pp.20661 - 20670-
dc.relation.isPartOfDESALINATION AND WATER TREATMENT-
dc.citation.titleDESALINATION AND WATER TREATMENT-
dc.citation.volume57-
dc.citation.number44-
dc.citation.startPage20661-
dc.citation.endPage20670-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalResearchAreaWater Resources-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.relation.journalWebOfScienceCategoryWater Resources-
dc.subject.keywordPlusMEMBRANE-CHARACTERISTICS-
dc.subject.keywordPlusTRANSPORT PARAMETERS-
dc.subject.keywordPlusENERGY-CONSUMPTION-
dc.subject.keywordPlusTEMPERATURE-
dc.subject.keywordPlusPERFORMANCE-
dc.subject.keywordPlusOPERATIONS-
dc.subject.keywordAuthorDesalination-
dc.subject.keywordAuthorNanofiltration-
dc.subject.keywordAuthorSWRO-
dc.subject.keywordAuthorDivalent ions-
dc.subject.keywordAuthorScaling-
dc.subject.keywordAuthorEnergy consumption-
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공과대학 (건축사회환경공학부)
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