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dc.contributor.author
D'ippolito, Silvana Andrea  
dc.contributor.author
Especel, Catherine  
dc.contributor.author
Epron, Florence  
dc.contributor.author
Pieck, Carlos Luis  
dc.date.available
2018-02-16T19:18:14Z  
dc.date.issued
2015-12  
dc.identifier.citation
D'ippolito, Silvana Andrea; Especel, Catherine; Epron, Florence; Pieck, Carlos Luis; Selective ring opening of methylcyclohexane and decalin over Rh-Pd supported catalysts: Effect of the preparation method; Elsevier; Fuel Processing Technology; 140; 12-2015; 180-187  
dc.identifier.issn
0378-3820  
dc.identifier.uri
http://hdl.handle.net/11336/36652  
dc.description.abstract
Bimetallic Rh-Pd catalysts prepared by various impregnation methods were evaluated in the selective ring-opening of decalin and methylcyclohexane (MCH) used as model molecules of hydrogenated aromatics of the Light Cycle Oil fraction. Rh and Pt were deposited on Al2O3 and SiO2-Al2O3 (S40) by coimpregnation (CI) or successive impregnations (SI) with different orders of metal addition. Catalysts were characterized by H2 chemisorption, temperature programmed reduction, temperature-programmed desorption of pyridine, and test reactions of cyclopentane hydrogenolysis and isomerization of 3,3-dimethyl-1-butene. Their catalytic behaviors for the ring-opening reaction were deeply influenced by the acidity of the support, and in a lesser extent by the metal deposition method. On both supports, the CI catalysts, displaying the highest dispersion values, exhibited the best ring opening performances. In the case of the SI catalysts, the addition order of both metals modified in a moderate way the properties of the catalyst. The yield to ring opening products obtained in MCH ring opening with CI catalysts supported on Al2O3 was 39-69% higher than those prepared by SI (conversion = 55-60%) while for the catalysts supported on S40, the yield to ring opening products was 8-48% higher for the CI catalysts compared to SI catalysts (conversion = 72-77%). The conversion of decalin for the bimetallic catalysts supported on Al2O3 was lower than 20% being dehydrogenated compounds the main reaction products regardless the preparation method. The catalyst supported on S40 showed decalin conversion values between 46-53% and yield to ring opening near to 30%. Moreover, the CI catalysts have yield to ring opening 10 to 20% higher than the catalysts prepared by SI. The catalyst prepared by coimpregnation supported on S40 was the most appropriate for opening the MCH and decalin due to an optimal balance between the metal and acid functions.  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
Elsevier  
dc.rights
info:eu-repo/semantics/openAccess  
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/  
dc.subject
Valorization of Lco  
dc.subject
Ring Opening of Naphthenes  
dc.subject
Methylcyclohexane  
dc.subject
Decalin  
dc.subject
Rh-Pd  
dc.subject
Silica-Alumina  
dc.subject.classification
Otras Ingeniería Química  
dc.subject.classification
Ingeniería Química  
dc.subject.classification
INGENIERÍAS Y TECNOLOGÍAS  
dc.title
Selective ring opening of methylcyclohexane and decalin over Rh-Pd supported catalysts: Effect of the preparation method  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2018-01-18T14:40:07Z  
dc.journal.volume
140  
dc.journal.pagination
180-187  
dc.journal.pais
Países Bajos  
dc.journal.ciudad
Amsterdam  
dc.description.fil
Fil: D'ippolito, Silvana Andrea. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina  
dc.description.fil
Fil: Especel, Catherine. Université de Poitiers; Francia  
dc.description.fil
Fil: Epron, Florence. Université de Poitiers; Francia  
dc.description.fil
Fil: Pieck, Carlos Luis. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina  
dc.journal.title
Fuel Processing Technology  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1016/j.fuproc.2015.08.027  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S0378382015301399