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dc.contributor.authorM. Gomez-
dc.contributor.authorM.D. Murcia-
dc.contributor.authorJ.L. Gomez-
dc.contributor.authorE. Gomez-
dc.contributor.authorM.F. Maximo-
dc.contributor.authorA. Garcia-
dc.contributor.otherFacultades, Departamentos, Servicios y Escuelas::Departamentos de la UMU::Ingeniería Químicaes
dc.date.accessioned2021-03-23T18:05:11Z-
dc.date.available2021-03-23T18:05:11Z-
dc.date.created2011-
dc.date.issued2012-
dc.identifier.citationApplied Catalysis B: Environmental, 117– 118 (2012) 194– 203es
dc.identifier.urihttp://hdl.handle.net/10201/105545-
dc.description© <2021>. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/ This document is the Accepted Manuscript version of a Published Work that appeared in final form in [Applied Catalysis B: Environmental]. To access the final edited and published work see [https://doi.org/10.1016/j.apcatb.2012.01.017].es
dc.description.abstractA KrCl exciplex flow-through photoreactor has been used for the removal of 4- chlorophenol. UV/H2O2 and photo-Fenton processes were tested. Considering the degradation of the different compounds, the molar ratio H2O2:4-chlorophenol did not show a significant influence on 4-chlorophenol while an optimum ratio of 25:1 was established for the photoproducts. The presence of the Fenton reagent led to a considerable improvement in the photodegradation of both the substrate and by- products, and an optimum Fe2+ concentration of 5 mg L-1 was determined. Under these conditions, total degradation was attained for a range of substrate concentrations between 50 and 150 mg L-1 and for reaction volumes of 500 mL. A photodegradation mechanism was also proposed, based on the formation of two intermediate compounds that quickly degrade to the primary photoproducts previously identified. A kinetic model was developed and theoretical conversion values of the 4-chlorophenol and the photoproducts were compared with the experimental ones, reaching a high degree of agreement (xcalc = 0.9964 xexp, R2 = 0.9986) and validating the proposed model. This system simulation using relatively high reaction volumes and including the by-products in the kinetic equations represents a first approach with a view to operating in continuous or semi-continuous systems that allow the scaling up of the process.es
dc.formatapplication/pdfes
dc.format.extent46es
dc.languageenges
dc.publisherElsevieres
dc.relationÁmbito del proyecto: Nacional Agencia/entidad financiadora: Ministerio de Ciencia e Innovación (MICINN) Convocatoria: Proyectos de Investigación Fundamental No Orientada 2010 Nombre del proyecto: Diseño, operación y modelización de un fotoproceso, basado en lámparas excimer de descarga en barrera, para la eliminación de contaminantes orgánicos de efluentes industriales Código: CTQ2010-17585es
dc.rightsinfo:eu-repo/semantics/openAccesses
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subject4-chlorophenoles
dc.subjectkinetic modeles
dc.subjectphotodegradationes
dc.subjectUVes
dc.subjectexcilampes
dc.subjectKrCl photoreactores
dc.subject.otherCDU::6 - Ciencias aplicadas::66 - Ingeniería, tecnología e industria química. Metalurgiaes
dc.titleA KrCl exciplex flow-through photoreactor for degrading 4-chlorophenol:Experimental and modellinges
dc.typeinfo:eu-repo/semantics/articlees
dc.identifier.doihttps://doi.org/10.1016/j.apcatb.2012.01.017-
Aparece en las colecciones:Artículos: Ingeniería Química

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