Solar photoelectro-Fenton treatment of a mixture of parabens spiked into secondary treated wastewater effluent at low input current

dc.contributor.authorSteter, Juliana R.
dc.contributor.authorBrillas, Enric
dc.contributor.authorSirés Sadornil, Ignacio
dc.date.accessioned2020-03-16T09:55:31Z
dc.date.issued2017-10-27
dc.date.updated2020-03-16T09:55:31Z
dc.description.abstractAqueous mixtures of methyl, ethyl and propyl paraben (MeP, EtP and PrP) prepared in real urban wastewater with low conductivity were treated by solar photoelectro-Fenton (SPEF) process at low input current (j = 10 mA cm-2) using a pre-pilot plant with an electrochemical reactor equipped with an air-diffusion cathode to electrogenerate H2O2 and a boron-doped diamond (BDD) or RuO2-based anode. Comparative trials in simulated water matrices with or without Cl− in the absence of natural organic matter (NOM) always led to a slower decay of parabens concentration and total organic carbon (TOC). This was mainly due to the superior regeneration of Fe2+ from photoreduction of Fe(III) complexes formed with NOM in real wastewater compared to that from Fe(OH)2+. In all matrices, a catalyst concentration as low as 0.20 mM Fe2+ was enough to ensure the production of ¿OH in the bulk from Fenton's reaction. SPEF with BDD yielded a complete removal of parabens in 180 min and 66% mineralization at 240 min. This gave rise to the greatest mineralization current efficiencies reported so far, up to 1000%, with a low energy consumption of 84 kWh (kg TOC)-1. The synergy between homogeneous and heterogeneous catalysis, which allowed the efficient dosage of ¿OH and M(¿OH) at low j, with simultaneous action of high UV power from sunlight justified such a good performance. Analogous apparent rate constants were determined for MeP, EtP and PrP. Slower decays were found with RuO2-based anode due to its lower oxidation power. As a result, the MCE was 425% as maximum, but a lower energy consumption of 52 kWh (kg TOC)-1 was needed. Since the role of active chlorine was of minor importance, the formation of toxic, refractory chloroderivatives was minimized. All by-products were transformed into malic, formic and oxalic acids prior to total mineralization.
dc.format.extent9 p.
dc.format.mimetypeapplication/pdf
dc.identifier.idgrec674140
dc.identifier.issn0926-3373
dc.identifier.urihttps://hdl.handle.net/2445/152797
dc.language.isoeng
dc.publisherElsevier B.V.
dc.relation.isformatofVersió postprint del document publicat a: https://doi.org/10.1016/j.apcatb.2017.10.060
dc.relation.ispartofApplied Catalysis B-Environmental, 2018, vol. 224, p. 410-418
dc.relation.urihttps://doi.org/10.1016/j.apcatb.2017.10.060
dc.rightscc-by-nc-nd (c) Elsevier B.V., 2018
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es
dc.sourceArticles publicats en revistes (Ciència dels Materials i Química Física)
dc.subject.classificationElectroquímica
dc.subject.classificationDepuració de l'aigua
dc.subject.otherElectrochemistry
dc.subject.otherWater purification
dc.titleSolar photoelectro-Fenton treatment of a mixture of parabens spiked into secondary treated wastewater effluent at low input current
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/acceptedVersion

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