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Water desalination by membrane distillation using PVDF-HFP hollow fiber membranes

dc.contributor.authorGarcía Payo, M. Carmen
dc.contributor.authorEssalhi, M.
dc.contributor.authorKhayet Souhaimi, Mohamed
dc.contributor.authorGarcía Fernández, L.
dc.contributor.authorCharfi, K.
dc.contributor.authorArafat, H.
dc.date.accessioned2023-06-20T03:42:52Z
dc.date.available2023-06-20T03:42:52Z
dc.date.issued2010-07
dc.descriptionThe author (M. Essalhi) is thankful to Middle East Desalination Research Centre (MEDRC) for the grant (Project 06-AS007). The authors also gratefully acknowledge the financial support of the Spanish Ministry of Science and Innovation (Project FIS2006-05323). The authors wish also to thank the financial support of the University Complutense of Madrid, UCM-BSCH (Project GR58/08, UCM group 910336).
dc.description.abstractPoly(vinylidene fluoride-co-hexafluoropropylene), PVDF-HFP, hollow fiber membranes were prepared by the dry/wet spinning technique using different polyethylene glycol (PEG) concentrations as non-solvent additive in the dope solution. Two different PEG concentrations (3 and 5 wt.%). The morphology and structural characteristics of the hollow fiber membranes were studied by means of optical microscopy, scanning electron microscopy, atomic force microscopy (AFM) and void volume fraction. The experimental permeate flux and the salt (NaCl) rejection factor were determined using direct contact membrane distillation (DCMD) process. An increase of the PEG content in the spinning solution resulted in a faster coagulation of the PVDF-HFP copolymer and a transition of the cross-section internal layer structure from a sponge-type structure to a finger-type structure. Pore size, nodule size and roughness parameters of both the internal and external hollow fiber surfaces were determined by AFM. It was observed that both the pore size and roughness of the internal surface of the hollow fibers enhanced with increasing the PEG concentration, whereas no change was observed at the outer surface. The void volume fraction increased with the increase of the PEG content in the spinning solution resulting in a higher DCMD flux and a smaller salt rejection factor.
dc.description.departmentDepto. de Estructura de la Materia, Física Térmica y Electrónica
dc.description.facultyFac. de Ciencias Físicas
dc.description.refereedTRUE
dc.description.sponsorshipMiddle East Desalination Research Centre (MEDRC)
dc.description.sponsorshipMinisterio de Ciencia e Innovación (MICINN)
dc.description.sponsorshipUniversity Complutense of Madrid, UCM-BSCH
dc.description.statuspub
dc.eprint.idhttps://eprints.ucm.es/id/eprint/26331
dc.identifier.doi10.12989/mwt.2010.1.3.215
dc.identifier.issn2005-8624
dc.identifier.officialurlhttp://dx.doi.org/10.12989/mwt.2010.1.3.215
dc.identifier.relatedurlhttp://koreascience.or.kr/
dc.identifier.urihttps://hdl.handle.net/20.500.14352/44303
dc.issue.number3
dc.journal.titleMembrane water treatment
dc.page.final230
dc.page.initial215
dc.publisherTechno-Press
dc.relation.projectID06-AS007
dc.relation.projectIDFIS2006-05323
dc.relation.projectIDGR58/08, UCM group 910336
dc.rights.accessRightsmetadata only access
dc.subject.cdu536
dc.subject.keywordWater treatment
dc.subject.keywordPoly(vinylidene fluoride-co-hexafluoropropylene)
dc.subject.keywordHollow fiber
dc.subject.keywordMembrane Distillation
dc.subject.ucmTermodinámica
dc.subject.unesco2213 Termodinámica
dc.titleWater desalination by membrane distillation using PVDF-HFP hollow fiber membranes
dc.typejournal article
dc.volume.number1
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