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Integrated direct contact membrane distillation for olive mill wastewater treatment

dc.contributor.authorEl-Abbassi, A.
dc.contributor.authorHafidi, A.
dc.contributor.authorKhayet Souhaimi, Mohamed
dc.contributor.authorGarcía Payo, M. Carmen
dc.date.accessioned2023-06-19T13:24:22Z
dc.date.available2023-06-19T13:24:22Z
dc.date.issued2013-08-15
dc.description© 2012 Elsevier B.V. The authors gratefully acknowledge the financial support of AECI (Agencia Espanola de Cooperacion Internacional, Ministerio de Asuntos Exteriores y de Cooperacion) through the projects A/023127/09 and A/032278/10.
dc.description.abstractDirect contact membrane distillation (DCMD) process was applied for olive mill wastewater (OMW) treatment and its concentration using a commercial flat-sheet polytetrafluoroethylene membrane (TF200, Gelman) with 0.2 mu m mean pore size. The effects of the mean temperature and temperature difference on the DCMD permeate flux were studied. Two pre-treatment processes, coagulation/flocculation and microfiltration (MF), were considered and the effects of each one on the DCMD performance were investigated. MF was found to be the optimum pre-treatment to be integrated to DCMD for OMW. When the permeate temperature was kept constant at 20 degrees C, the DCMD permeate flux increased with the increase of the feed temperature. However, the permeate flux decreased with the feed phenol concentration of OMW. The concentration factor of each phenolic compound varied from 1.56 to 2.93. The main phenolic compound in the tested OMW samples was found to be the hydroxytyrosol, which was concentrated more than two times from 4.01 g/L to 8.16 g/L after 40 h of OMW processing by DCMD. The membrane fouling phenomenon was also studied. Results showed that the integrated MF/DCMD can be an effective process for the treatment and concentration of OMW obtaining clean water and a phenolic-rich concentrate.
dc.description.departmentDepto. de Estructura de la Materia, Física Térmica y Electrónica
dc.description.facultyFac. de Ciencias Físicas
dc.description.refereedTRUE
dc.description.sponsorshipAECI (Agencia Española de Cooperación Internacional, Ministerio de Asuntos Exteriores y de Cooperación)
dc.description.statuspub
dc.eprint.idhttps://eprints.ucm.es/id/eprint/25794
dc.identifier.doi10.1016/j.desal.2012.06.014
dc.identifier.issn0011-9164
dc.identifier.officialurlhttp://dx.doi.org/10.1016/j.desal.2012.06.014
dc.identifier.relatedurlhttp://www.sciencedirect.com/
dc.identifier.urihttps://hdl.handle.net/20.500.14352/33567
dc.journal.titleDesalination
dc.language.isoeng
dc.page.final38
dc.page.initial31
dc.publisherElsevier Science Bv
dc.relation.projectIDA/023127/09
dc.relation.projectIDA/032278/10
dc.rights.accessRightsrestricted access
dc.subject.cdu536
dc.subject.keywordPhenolic-compounds
dc.subject.keywordAnaerobic-digestion
dc.subject.keywordPolyphenols
dc.subject.keywordWastewaters
dc.subject.keywordFractionation
dc.subject.keywordRecovery
dc.subject.keywordSystem
dc.subject.keywordDecolourization
dc.subject.keywordAntioxidants
dc.subject.keywordRemoval
dc.subject.ucmTermodinámica
dc.subject.unesco2213 Termodinámica
dc.titleIntegrated direct contact membrane distillation for olive mill wastewater treatment
dc.typejournal article
dc.volume.number323
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