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dc.contributor.author
Di Luca, Carla
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dc.contributor.author
Massa, Paola Andrea
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dc.contributor.author
Fenoglio, Rosa Juana
dc.contributor.author
Medina Cabello, Francisco
dc.date.available
2016-02-26T16:23:55Z
dc.date.issued
2014-05-29
dc.identifier.citation
Di Luca, Carla; Massa, Paola Andrea; Fenoglio, Rosa Juana; Medina Cabello, Francisco; Improved Fe2O3/Al2O3 as heterogeneous Fenton catalysts for the oxidation of phenol solutions in a continuous reactor; John Wiley & Sons Ltd; Journal Of Chemical Technology And Biotechnology; 89; 8; 29-5-2014; 1121-1128
dc.identifier.issn
0268-2575
dc.identifier.uri
http://hdl.handle.net/11336/4457
dc.description.abstract
Improved Fe2O3/Al2O3 catalysts were studied for the catalytic oxidation of concentrated phenol solutions (5 g L−1) with H2O2. To enhance catalyst stability, two strategies were investigated: the use of a high calcination temperature and a step of immersion into an organic acid solution. The reaction runs were performed in a continuous reactor at 70°C and atmospheric pressure.
RESULTS: For all the catalysts, almost complete phenol degradation was achieved. The mineralization levels were incomplete, reaching 60 and 50% for the catalysts treated with acetic and oxalic acid, respectively. The leaching levels were reduced from 25% (for the untreated catalyst) to 11% after the immersion in oxalic acid. In all cases, the formation of reversible carbonaceous deposits was observed during reaction and a progressive decay in phenol, TOC and H2O2 conversions was registered.
CONCLUSION:Catalyst resistance to leaching was significantly enhanced by combining both thermal and acidic treatments. These procedures did not affect the catalytic wet hydrogen peroxide oxidation (CWHPO) performance in terms of mineralization levels. The lixiviation levels were acceptable, taking into account the strong acidic reaction medium. Deactivation processes might be primarily associated with the formation of reversible carbonaceous deposits due to intermediates accumulation onto the catalyst surface.
dc.format
application/pdf
dc.language.iso
eng
dc.publisher
John Wiley & Sons Ltd
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dc.rights
info:eu-repo/semantics/openAccess
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.subject
Cwhpo
dc.subject
Fe2o3/Alumina
dc.subject
Fenton-Like Reaction
dc.subject
Phenol Removal
dc.subject.classification
Ingeniería de Procesos Químicos
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dc.subject.classification
Ingeniería Química
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dc.subject.classification
INGENIERÍAS Y TECNOLOGÍAS
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dc.title
Improved Fe2O3/Al2O3 as heterogeneous Fenton catalysts for the oxidation of phenol solutions in a continuous reactor
dc.type
info:eu-repo/semantics/article
dc.type
info:ar-repo/semantics/artículo
dc.type
info:eu-repo/semantics/publishedVersion
dc.date.updated
2016-03-30 10:35:44.97925-03
dc.journal.volume
89
dc.journal.number
8
dc.journal.pagination
1121-1128
dc.journal.pais
Reino Unido
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dc.journal.ciudad
Oxford
dc.description.fil
Fil: Di Luca, Carla. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Mar del Plata. Instituto de Investigación En Ciencia y Tecnología de Materiales (i); Argentina. Universidad Nacional de Mar del Plata. Facultad de Ingeniería; Argentina
dc.description.fil
Fil: Massa, Paola Andrea. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Mar del Plata. Instituto de Investigación En Ciencia y Tecnología de Materiales (i); Argentina. Universidad Nacional de Mar del Plata. Facultad de Ingeniería; Argentina
dc.description.fil
Fil: Fenoglio, Rosa Juana. Universidad Nacional de Mar del Plata; Argentina
dc.description.fil
Fil: Medina Cabello, Francisco. Universitat Rovira I Virgili; España
dc.journal.title
Journal Of Chemical Technology And Biotechnology
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dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/10.1002/jctb.4412
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/http://onlinelibrary.wiley.com/doi/10.1002/jctb.4412/abstract
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1002/jctb.4412
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