Seawater desalination by using nanofiltration (NF) and brackish water reverse osmosis (BWRO) membranes in sequential mode of operation

dc.authorscopusid56190087100
dc.authorscopusid57201457166
dc.authorscopusid57212865806
dc.authorscopusid35795160600
dc.authorscopusid7004128490
dc.authorscopusid6602100613
dc.authorscopusid6602100613
dc.contributor.authorKaya,C.
dc.contributor.authorJarma,Y.A.
dc.contributor.authorMuhidin,A.M.
dc.contributor.authorGüler,E.
dc.contributor.authorKabay,N.
dc.contributor.authorArda,M.
dc.contributor.authorYüksel,M.
dc.contributor.otherLaw
dc.contributor.otherChemical Engineering
dc.date.accessioned2024-07-05T15:45:55Z
dc.date.available2024-07-05T15:45:55Z
dc.date.issued2020
dc.departmentAtılım Universityen_US
dc.department-tempKaya C., Ege University, Faculty of Engineering, Department of Chemical Engineering, Izmir, Turkey, Ege University, Faculty of Science, Department of Chemistry, Izmir, Turkey; Jarma Y.A., Ege University, Faculty of Engineering, Department of Chemical Engineering, Izmir, Turkey; Muhidin A.M., Ege University, Faculty of Engineering, Department of Chemical Engineering, Izmir, Turkey; Güler E., Atilim University, Faculty of Engineering, Department of Chemical Engineering and Applied Chemistry, Ankara, Turkey; Kabay N., Ege University, Faculty of Engineering, Department of Chemical Engineering, Izmir, Turkey; Arda M., Ege University, Faculty of Science, Department of Chemistry, Izmir, Turkey; Yüksel M., Ege University, Faculty of Engineering, Department of Chemical Engineering, Izmir, Turkeyen_US
dc.description.abstractIn this study, the applicability of nanofiltration (NF) membranes as a pretreatment prior to reverse osmosis (RO) in seawater desalination was investigated. The membranes used were NF270 and NF90 as the NF membranes, while the brackish water (BW) RO membrane BW30 was used as the RO membrane. In desalination tests, permeates of the NF membranes were collected and used as the feed to the BW30 membrane. The calculated permeate fluxes were 6.7 L/h.m2, 11.3 L/h.m2, 24.3 L/h.m2, and 36.6 L/h.m2 for single BW30-35 bar, NF270-30 bar + BW30-35 bar, NF90-30 bar + BW30-25 bar and NF90-30 BW30-35 bar, respectively. The calculated water recovery and rejected salt values were 51.6%, 41.4%, 24.8%, 15.4% and 98.2%, 98.2%, 96.0%, 91.0% for NF90-30 bar + BW30-35 bar, NF90-30 bar + BW30-25 bar, NF270-30 bar + BW30-35 bar and single BW30-35 bar, respectively. The qualities of the product waters of integrated systems (NF+BWRO) and the single BWRO system were also investigated. Boron rejection was fairly well with average boron rejections of 59.3% and 60.2% by NF90-30 bar + BW30-25 bar and NF90-30 bar + BW30-35 bar combinations, respectively while single BW30-35 bar gave an average rejection of 49.6%. The results obtained showed that the quality of product water obtained using single BWRO did not comply with the irrigation standards, while the integrated systems provided total compliance to irrigation standards with the exception of boron. © 2020 MPRL. All rights reserved.en_US
dc.description.sponsorshipAliye USTER Foundation; Ege Üniversitesi, (2013-FEN-061)en_US
dc.identifier.citation19
dc.identifier.doi10.22079/JMSR.2019.107844.1264
dc.identifier.endpage46en_US
dc.identifier.issn2476-5406
dc.identifier.issue1en_US
dc.identifier.scopus2-s2.0-85077447814
dc.identifier.startpage40en_US
dc.identifier.urihttps://doi.org/10.22079/JMSR.2019.107844.1264
dc.identifier.urihttps://hdl.handle.net/20.500.14411/3977
dc.identifier.volume6en_US
dc.institutionauthorYüksel, Melis
dc.institutionauthorGüler, Enver
dc.language.isoenen_US
dc.publisherAmirkabir University of Technology - Membrane Processes Research Laboratoryen_US
dc.relation.ispartofJournal of Membrane Science and Researchen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectDesalinationen_US
dc.subjectIntegrated systemen_US
dc.subjectNanofiltrationen_US
dc.subjectReverse osmosisen_US
dc.subjectSeawateren_US
dc.titleSeawater desalination by using nanofiltration (NF) and brackish water reverse osmosis (BWRO) membranes in sequential mode of operationen_US
dc.typeArticleen_US
dspace.entity.typePublication
relation.isAuthorOfPublication05cb66bf-04c9-4744-be69-83cf03cf5db3
relation.isAuthorOfPublicationcf7476e1-9efa-4710-a516-dbabb21b6e1a
relation.isAuthorOfPublication.latestForDiscovery05cb66bf-04c9-4744-be69-83cf03cf5db3
relation.isOrgUnitOfPublicatione40fcdbb-ea25-46e4-bd15-a253c340196a
relation.isOrgUnitOfPublicationbebae599-17cc-4f0b-997b-a4164a19b94b
relation.isOrgUnitOfPublication.latestForDiscoverye40fcdbb-ea25-46e4-bd15-a253c340196a

Files

Collections