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dc.contributor.author
Bocanegra, Sonia Alejandra
dc.contributor.author
Guerrero Ruiz, A.
dc.contributor.author
Scelza, Osvaldo Antonio
dc.contributor.author
de Miguel, Sergio Ruben
dc.date.available
2017-07-21T16:03:32Z
dc.date.issued
2013-01
dc.identifier.citation
Bocanegra, Sonia Alejandra; Guerrero Ruiz, A.; Scelza, Osvaldo Antonio; de Miguel, Sergio Ruben; MgAl2O4 spinel prepared by novel mechanochemical synthesis used as a support of multimetallic catalysts for paraffin dehydrogenation; Pleiades Publishing; Catalysis in Industry; 5; 1; 1-2013; 61-73
dc.identifier.issn
2070-0504
dc.identifier.uri
http://hdl.handle.net/11336/21068
dc.description.abstract
The catalytic performance in nbutane dehydrogenation of bimetallic PtSn, PtGa and PtIn, and tri metallic PtSnIn and PtSnGa catalysts (with low metal contents) supported on a MgAl2O4 prepared by a novel mechanochemical synthesis was evaluated both in flow and pulse equipment. The influence of the addition of different promoters (Sn, Ga and In) to Pt on the activity, selectivity and deactivation in the nbutane dehydro genation reaction was studied. Stability experiments through successive reactionregeneration cycles were car ried out for selected catalysts. In order to correlate the properties of the metallic phase of the catalysts with the catalytic behavior, several characterization techniques were used, such as test reactions of the metallic phase (cyclohexane dehydrogenation and cyclopentane hydrogenolysis), TPR, XPS, H2 chemisorption and TEM. Bimetallic PtSn catalyst has a better catalytic behavior than PtIn and PtGa ones. For PtSnM (M: In or Ga) cat alysts, whereas Ga addition to the bimetallic catalyst does not practically modify the dehydrogenation perform ance, the addition of In produces an increase of the activity and the selectivity to butenes. Characterization results indicate the presence of geometric effects for the PtSn catalyst, and geometric and electronic effects for PtIn and PtGa ones. For trimetallic catalysts, the presence of a close contact between Pt, Sn and In or Ga in both trimetallic catalysts was found, mainly due to geometric effects like blocking and dilution of the active sites by the promoters. In stability experiments, the trimetallic PtSnIn/MgAl2O4 catalyst clearly displays the best cat alytic performance along reactionregeneration cycles, though PtSnGa and PtSn catalysts also showed a very good behavior through the successive cycles. The characterization of these catalysts after cycles shows that their metallic phases are slightly modified along the cycles.
dc.format
application/pdf
dc.language.iso
eng
dc.publisher
Pleiades Publishing
dc.rights
info:eu-repo/semantics/openAccess
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.subject
Paraffin Dehydrogenation
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Mgal2o4 Support
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Mechanochemical Synthesis
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Ptsnin And Ptsnga Supported Catalysts
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Characterization of Supported Catalysts
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Otras Ingeniería Química
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Ingeniería Química
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INGENIERÍAS Y TECNOLOGÍAS
dc.title
MgAl2O4 spinel prepared by novel mechanochemical synthesis used as a support of multimetallic catalysts for paraffin dehydrogenation
dc.type
info:eu-repo/semantics/article
dc.type
info:ar-repo/semantics/artículo
dc.type
info:eu-repo/semantics/publishedVersion
dc.date.updated
2017-07-19T20:35:09Z
dc.identifier.eissn
2070-0555
dc.journal.volume
5
dc.journal.number
1
dc.journal.pagination
61-73
dc.journal.pais
Rusia
dc.description.fil
Fil: Bocanegra, Sonia Alejandra. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones En Catalisis y Petroquímica "ing. Jose Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones En Catalisis y Petroquímica "ing. Jose Miguel Parera"; Argentina
dc.description.fil
Fil: Guerrero Ruiz, A.. Universidad Nacional de Educación a distancia. Facultad de Ciencias. Departamento de Química Inorgánica y Química Técnica; España
dc.description.fil
Fil: Scelza, Osvaldo Antonio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones En Catalisis y Petroquímica "ing. Jose Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones En Catalisis y Petroquímica "ing. Jose Miguel Parera"; Argentina
dc.description.fil
Fil: de Miguel, Sergio Ruben. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones En Catalisis y Petroquímica "ing. Jose Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones En Catalisis y Petroquímica "ing. Jose Miguel Parera"; Argentina
dc.journal.title
Catalysis in Industry
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1134/S2070050413010030
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://link.springer.com/article/10.1134%2FS2070050413010030
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