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Authordc.contributor.authorSalinas, Daniela 
Authordc.contributor.authorGuerrero, Sichem es_CL
Authordc.contributor.authorAraya Figueroa, Paulo es_CL
Admission datedc.date.accessioned2010-07-01T18:25:22Z
Available datedc.date.available2010-07-01T18:25:22Z
Publication datedc.date.issued2010
Cita de ítemdc.identifier.citationCatalysis Communications 11 (2010) 773–777en_US
Identifierdc.identifier.otherdoi:10.1016/j.catcom.2010.02.013
Identifierdc.identifier.urihttps://repositorio.uchile.cl/handle/2250/125385
Abstractdc.description.abstractThe transesterification reaction of canola oil was studied on titania-supported catalysts with varying loadings of potassium. It was found that the most active catalysts fall in the range where the adsorption/ desorption of CO2 was the highest. Total conversion to methyl esters was achieved on a catalyst with 20% K-loading under air conditions and with no in situ pre-treatment before reaction.en_US
Patrocinadordc.description.sponsorshipThe funding from the CIMAT project No. 11980002 is gratefully acknowledged for funding this work.en_US
Lenguagedc.language.isoenen_US
Publisherdc.publisherELSEVIERen_US
Keywordsdc.subjectHeterogeneous transesterificationen_US
Títulodc.titleTransesterification of canola oil on potassium-supported TiO2 catalystsen_US
Document typedc.typeArtículo de revista


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