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dc.contributor.author
Segobia, Dario Jobino  
dc.contributor.author
Trasarti, Andres Fernando  
dc.contributor.author
Apesteguia, Carlos Rodolfo  
dc.date.available
2023-01-12T10:26:58Z  
dc.date.issued
2021-11  
dc.identifier.citation
Segobia, Dario Jobino; Trasarti, Andres Fernando; Apesteguia, Carlos Rodolfo; Highly selective production of benzylamine from benzonitrile on metal-supported catalysts; Royal Society of Chemistry; Reaction Chemistry and Engineering; 6; 11; 11-2021; 2181-2190  
dc.identifier.issn
2058-9883  
dc.identifier.uri
http://hdl.handle.net/11336/184456  
dc.description.abstract
The selective liquid-phase hydrogenation of benzonitrile (BeN) to benzylamine (BeA) was investigated on silica-supported Ni, Co and Pd catalysts at 373 K and 13 bar H2, using ethanol as a solvent. Ni/SiO2 was more active and selective to BeA than Co/SiO2 and Pd/SiO2, yielding 78% of BeA and dibenzylamine (DBeA) as the only byproduct. The reaction was of positive order with respect to H2 and BeN on Ni/SiO2, but the selectivity to BeA did not change by increasing the reactant concentrations. In contrast, the BeA selectivity increased with the temperature. The effect of solvent on Ni/SiO2 activity and selectivity was studied by using non-polar aromatic (toluene) and naphthenic (cyclohexane) hydrocarbons, and protic alcohols (methanol, ethanol). The highest BeA yield (92%) was obtained in methanol, without the addition of any additives. Ni/SiO2 may be regenerated and reused after reaction, maintaining its catalytic selectivity performance at full BeN conversion.  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
Royal Society of Chemistry  
dc.rights
info:eu-repo/semantics/restrictedAccess  
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/  
dc.subject
benzonitrile  
dc.subject.classification
Ingeniería de Procesos Químicos  
dc.subject.classification
Ingeniería Química  
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INGENIERÍAS Y TECNOLOGÍAS  
dc.title
Highly selective production of benzylamine from benzonitrile on metal-supported catalysts  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2022-09-21T23:26:41Z  
dc.journal.volume
6  
dc.journal.number
11  
dc.journal.pagination
2181-2190  
dc.journal.pais
Países Bajos  
dc.journal.ciudad
Amsterdam  
dc.description.fil
Fil: Segobia, Dario Jobino. 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: Trasarti, Andres Fernando. 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: Apesteguia, Carlos Rodolfo. 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.journal.title
Reaction Chemistry and Engineering  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1039/d1re00234a  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://pubs.rsc.org/en/content/articlelanding/2021/RE/D1RE00234A