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dc.contributor.author
Fonseca, Juliana Da Silva Lima  
dc.contributor.author
Júnior, Arnaldo Da Costa Faro  
dc.contributor.author
Grau, Javier Mario  
dc.contributor.author
Rangel, Maria do Carmo  
dc.date.available
2018-08-02T23:45:45Z  
dc.date.issued
2010-09  
dc.identifier.citation
Fonseca, Juliana Da Silva Lima; Júnior, Arnaldo Da Costa Faro; Grau, Javier Mario; Rangel, Maria do Carmo; Ethylbenzene production over platinum catalysts supported on modified KY zeolites; Elsevier Science; Applied Catalysis A: General; 386; 9-2010; 201-210  
dc.identifier.issn
0926-860X  
dc.identifier.uri
http://hdl.handle.net/11336/54027  
dc.description.abstract
Platinum catalysts supported on zeolite KY (Si/Al = 12.7), modified with magnesium, calcium or barium, were evaluated in n-octane reforming to produce ethylbenzene. The catalysts were characterized by nitrogen adsorption, 27Al and 29Si solid state nuclear magnetic resonance, Fourier transform infrared spectroscopy using carbon monoxide or pyridine, metal dispersion measurements and programmed temperature oxidation. No significant structural change was noted for the solids due to the dopants except<br />for barium, which decreased the specific surface area, due to the partial blockage of the zeolite channels by the large size ions. However, a decrease was noted for all samples due to platinum, which partially blocked the zeolite channels. Barium also decreased the crystallinity while platinum caused this effect only for calcium and barium-containing samples, due to the structure partial collapse. Metallic platinum species in several electronic states were detected in the cages of zeolite, barium-containing catalyst showing the most electron-enriched platinum atoms. The amount of Lewis and Brønsted acid sites increased due to magnesium and calcium but barium increased only the amount of Lewis acid sites, as compared to potassium-containing solid. The catalysts with magnesium and barium showed the same platinum dispersion, which was higher than the one containing calcium. All catalysts were active in n-octane reforming at 723K and selective to ethylbenzene, but the conversion dropped with time reaction due to the decrease of specific surface area and to coke deposition. The calcium-containing sample produced the hardest coke, which led to the highest drop in conversion. The n-octane conversion was supposed to occur by a monofunctional mechanism but the bifunctional mechanism also seemed to occur due to the residual acidity of the catalysts. The calcium and barium-containing catalysts were the most selective to<br />ethylbenzene, due to electron-enriched platinum species related to promoters, but the low ethylbenzene selectivity for the magnesium-containing catalyst was compensated by its high conversion, resulting in similar yields for all catalysts.  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
Elsevier Science  
dc.rights
info:eu-repo/semantics/openAccess  
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/  
dc.subject
N-Octane Reforming  
dc.subject
Y Zeolite  
dc.subject
Ethylbenzene  
dc.subject
Coke  
dc.subject
Barium  
dc.subject
Calcium  
dc.subject
Magnesium  
dc.subject.classification
Otras Ciencias Químicas  
dc.subject.classification
Ciencias Químicas  
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CIENCIAS NATURALES Y EXACTAS  
dc.title
Ethylbenzene production over platinum catalysts supported on modified KY zeolites  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2018-07-31T17:35:38Z  
dc.journal.volume
386  
dc.journal.pagination
201-210  
dc.journal.pais
Países Bajos  
dc.journal.ciudad
Amsterdam  
dc.description.fil
Fil: Fonseca, Juliana Da Silva Lima. Universidade Federal da Bahia; Brasil  
dc.description.fil
Fil: Júnior, Arnaldo Da Costa Faro. Universidade Federal do Rio de Janeiro; Brasil  
dc.description.fil
Fil: Grau, Javier Mario. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; Argentina  
dc.description.fil
Fil: Rangel, Maria do Carmo. Universidade Federal da Bahia; Brasil  
dc.journal.title
Applied Catalysis A: General  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1016/j.apcata.2010.07.056