Modified diatomites for Fenton-like oxidation of phenol

Raw diatomites were modified by acid or base treatments; addition of Fe or Cu species through the incipient wet impregnation method (IWI) and calcination at 700 °C. Samples were characterized by X-ray powder diffraction (XRD), scanning electron microscopy (SEM-EDX), Mossbauer spectroscopy, point of...

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Detalles Bibliográficos
Autores: Inchaurrondo, Natalia Soledad, Ramos, Cinthia Paula, Zerjav, G., Font, J., Pintar, A., Haure, Patricia Monica
Tipo de recurso: artículo
Estado:Versión publicada
Fecha de publicación:2016
País:Argentina
Institución:Consejo Nacional de Investigaciones Científicas y Técnicas
Repositorio:CONICET Digital (CONICET)
Idioma:inglés
OAI Identifier:oai:ri.conicet.gov.ar:11336/32555
Acceso en línea:http://hdl.handle.net/11336/32555
Access Level:acceso abierto
Palabra clave:Diatomites
Phenol
Natural Catalyst
Fenton-like
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
Descripción
Sumario:Raw diatomites were modified by acid or base treatments; addition of Fe or Cu species through the incipient wet impregnation method (IWI) and calcination at 700 °C. Samples were characterized by X-ray powder diffraction (XRD), scanning electron microscopy (SEM-EDX), Mossbauer spectroscopy, point of zero charge (PZC), pyridine temperature programme desorption (TPD), themogravimetric analysis (TGA) and BET surface area determination. According to characterization results, four samples were selected: simply calcined Diatom (D), iron added (Fe-D), acid treated Fe reimpregnated (H-Fe-D) and copper added (Cu/Fe-D). Materials were tested as catalysts for the peroxidation of phenol solutions (1000 mg/L) in a batch laboratory reactor, at different operating conditions in 5 h tests. D, Fe-D and H-Fe-D samples allowed complete phenol removal under all the operating range studied. At optimum conditions, TOC conversions of 50–55% were obtained. Metal ions added through the IWI procedure resulted more labile than metal present originally. The acidic treatment favored the initiation of the reaction showing a reduction of the induction period at almost neutral initial pH. The Fe-D catalyst exhibited poor performance, lower reactions rates and higher Fe leaching. Conversely, high TOC conversions (80%) were achieved with Cu/Fe-D, however, Cu leaching was excessive (12.7%). D and H-Fe-D samples were used in consecutive runs (up to 20 h) maintaining phenol conversion and TOC reduction. Overall, a good performance was obtained, even comparable to more sophisticated Fe catalysts.