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Wet Peroxide Oxidation of Chlorobenzenes Catalyzed by Goethite and Promoted by Hydroxylamine

dc.contributor.authorLorenzo Fernández, David
dc.contributor.authorDomínguez Torre, Carmen María
dc.contributor.authorRomero, Arturo
dc.contributor.authorSantos López, Aurora
dc.date.accessioned2023-06-17T12:36:04Z
dc.date.available2023-06-17T12:36:04Z
dc.date.issued2019-06-20
dc.description.abstractIn this work, the abatement of several chlorobenzenes commonly found as pollutants in the aqueous phase has been carried out by catalytic wet peroxide oxidation using goethite as the catalyst and hydroxylamine as the promotor. Spiked water with monochlorobenzene and different positional isomers of dichlorobenzene, trichlorobenzene, and tetrachlorobenzene, at concentrations ranging from 0.4 to 16.9 mg L−1 was treated. Runs were carried out batch-way, at room conditions, without headspace. The heterogeneous catalyst was commercial goethite, with a specific surface area (SBET) of 10.24 m2 g−1 and a total iron content of 57.3 wt%. Iron acts as a catalyst of hydrogen peroxide decomposition to hydroxyl radicals. Hydroxylamine (in a range from 0 to 4.9 mM) was added to enhance the iron redox cycle from Fe (III) to Fe (II), remarkably increasing the radical production rate and therefore, the conversion of chlorobenzenes. Iron was stable (not leached to the aqueous phase) even at the lowest pH tested (pH = 1). The effect of pH (from 2 to 7), hydrogen peroxide (from 1 to 10 times the stoichiometric dosage), hydroxylamine, and catalyst concentration (from 0.25 to 1 g/L) was studied. Pollutant removal increased with hydroxylamine and hydrogen peroxide concentration. An operating conditions study demonstrated that the higher the hydroxylamine and hydrogen peroxide concentrations, the higher the removal of pollutants. The optimal pH value and catalyst concentration was 3 and 0.5 g L−1, respectively. Operating with 2.4 mM of hydroxylamine and 10 times the stoichiometric H2O2 amount, a chlorobenzenes conversion of 90% was achieved in 2.5 h. Additionally, no toxic byproducts were obtained.
dc.description.departmentDepto. de Ingeniería Química y de Materiales
dc.description.facultyFac. de Ciencias Químicas
dc.description.refereedTRUE
dc.description.sponsorshipMinisterio de Economía y Competitividad (MINECO)
dc.description.sponsorshipComunidad de Madrid
dc.description.statuspub
dc.eprint.idhttps://eprints.ucm.es/id/eprint/66150
dc.identifier.doi10.3390/catal9060553
dc.identifier.issn2073-4344
dc.identifier.officialurlhttps://doi.org/10.3390/catal9060553
dc.identifier.relatedurlhttps://www.mdpi.com/2073-4344/9/6/553
dc.identifier.urihttps://hdl.handle.net/20.500.14352/12593
dc.issue.number6
dc.journal.titleCatalysts
dc.language.isoeng
dc.page.initial553
dc.publisherMDPI
dc.relation.projectIDCTM2016-77151-C2-1-R
dc.relation.projectIDCARESOIL-CM (S2018/EMT-4317)
dc.rightsAtribución 3.0 España
dc.rights.accessRightsopen access
dc.rights.urihttps://creativecommons.org/licenses/by/3.0/es/
dc.subject.keywordchlorobenzenes
dc.subject.keywordgoethite
dc.subject.keywordcatalytic wet peroxide oxidation
dc.subject.keywordhydroxylamine
dc.subject.keywordiron redox cycle
dc.subject.ucmIngeniería química
dc.subject.unesco3303 Ingeniería y Tecnología Químicas
dc.titleWet Peroxide Oxidation of Chlorobenzenes Catalyzed by Goethite and Promoted by Hydroxylamine
dc.typejournal article
dc.volume.number9
dspace.entity.typePublication
relation.isAuthorOfPublication53b0ff5e-06e0-4b3f-b275-983b7944879f
relation.isAuthorOfPublicationed6e75ce-3c05-40f4-9238-3e4743fe1385
relation.isAuthorOfPublicationc9d0900f-4c0e-4a20-867d-8103d0ac678a
relation.isAuthorOfPublication.latestForDiscovery53b0ff5e-06e0-4b3f-b275-983b7944879f

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