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dc.contributor.authorSoriano Portilla, Álvaro
dc.contributor.authorSchaefer, Charles E.
dc.contributor.authorUrtiaga Mendia, Ana María 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2021-01-25T13:49:36Z
dc.date.available2021-01-25T13:49:36Z
dc.date.issued2020-12-15
dc.identifier.issn2666-8211
dc.identifier.otherCTM2016-75509-Res_ES
dc.identifier.otherPID2019-105827RB-I00es_ES
dc.identifier.urihttp://hdl.handle.net/10902/20537
dc.description.abstractThis work explores the treatment of poly- and perfluoroalkyl acids (PFAAs) in groundwater by coupling membrane separation and electrochemical oxidation (ELOX). A process system engineering approach based on modelling and empirical data was followed. Two nanofiltration (NF90) and reverse osmosis (BW30) membranes were characterized for treating an electrolyte (NaCl and CaSO4) mixture of perfluorocarboxylic acids (PFCAs) containing PFOA, PFHpA, PFHxA, PFPeA and PFBA with initial concentrations of 10 µg L−1 each. Membrane surface charge shielding and concentration polarization negatively influenced NF90 performance, and the BW30 membrane was selected. Electrochemical oxidation with boron doped diamond anodes treated the PFCAs mixture amended with PFOS and 6:2 FTSA, emulating previously pre-concentrated feed and non-preconcentrated feed conditions. Working at different current densities (J) between 20 and 350 A m−2, the removal of PFOA, PFOS and 6:2 FTSA followed first order apparent kinetics, although shorter chain PFCAs initially showed increasing trends because of their simultaneous electrogeneration and degradation. Overall, ΣPFAA electrolysis followed first order kinetics linearly correlated to J in the full range of testing. Unexpectedly, PFAAs electrolysis was faster for the low conductive non-preconcentrated feed, a result that was ascribed to the enhanced direct electron transfer mechanism resulting from the higher cell voltage. For 99.9% PFAAs removal, the total specific cost of treatment was minimized using a cascade of four RO stages and ELOX treatment of the concentrate, to reach ΣPFAA below the Health Advisory Levels recommended by the USEPA in drinking water (<70 ng L−1 sum of PFOA and PFOS).es_ES
dc.description.sponsorshipFinancial support by the Spanish Ministry of Economy and Compet- itiveness through projects CTM2016-75509-R (MINECO, SPAIN-FEDER 2014-2020) and PID2019-105827RB-I00 (AEI, Spain) is gratefully acknowledged.es_ES
dc.format.extent9 p.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 International. ©The Author(s). Published by Elsevier B.V.es_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.sourceChemical Engineering Journal Advances, 2020, 4, 100042es_ES
dc.subject.otherPFOAes_ES
dc.subject.otherPFOSes_ES
dc.subject.otherElectrooxidationes_ES
dc.subject.otherReverse osmosises_ES
dc.subject.otherEconomic evaluationes_ES
dc.titleEnhanced treatment of perfluoroalkyl acids in groundwater by membrane separation and electrochemical oxidationes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.ceja.2020.100042es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.ceja.2020.100042
dc.type.versionpublishedVersiones_ES


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Attribution-NonCommercial-NoDerivatives 4.0 International. ©The Author(s). Published by Elsevier B.V.Excepto si se señala otra cosa, la licencia del ítem se describe como Attribution-NonCommercial-NoDerivatives 4.0 International. ©The Author(s). Published by Elsevier B.V.