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dc.contributor.authorÁlvarez Montero, Ariadna 
dc.contributor.authorMartín-Martinez, Maria
dc.contributor.authorGómez Sainero, Luisa María 
dc.contributor.authorArevalo-Bastante, Alejandra
dc.contributor.authorBedia García-Matamoros, Jorge 
dc.contributor.authorRodriguez, Juan J.
dc.contributor.otherUAM. Departamento de Química Física Aplicadaes_ES
dc.date.accessioned2016-11-23T11:41:03Z
dc.date.available2016-11-23T11:41:03Z
dc.date.issued2015-02-25
dc.identifier.citationIndustrial and Engineering Chemistry Research 54.7 (2015): 2023-2029en_US
dc.identifier.issn0888-5885es_ES
dc.identifier.urihttp://hdl.handle.net/10486/675389
dc.descriptionThis document is the unedited author's version of a Submitted Work that was subsequently accepted for publication in Industrial and Engineering Chemistry Research, copyright © American Chemical Society after peer review. To access the final edited and published work, see http://pubs.acs.org/doi/abs/10.1021/ie5042484en_US
dc.description.abstractThe kinetics of the hydrodechlorination (HDC) of dichloromethane (DCM) and chloroform (TCM) with Pd, Pt, Rh, and Ru on activated carbon catalysts has been studied at temperatures between 100 and 250 °C. Different kinetic models have been checked, namely, pseudo-first-order and Langmuir-Hinshelwood-Hougen-Watson (LHHW) with adsorption, chemical reaction, or desorption control. The HDC of DCM and TCM with the Pd and Pt catalysts was well-described by the LHHW model with reactant adsorption as the rate-controlling step. However, with Rh and Ru catalysts, chemical reaction and desorption of the reaction products appear to be the rate-controlling steps in the HDC of DCM and TCM, respectively. In this last case, different sets of complex reactions seem to occur on the surface of the catalyst depending on the temperature, preventing determination of a confident value of the activation energy, because of the formation of oligomeric coke-like deposits and the subsequent severe deactivation of these catalysts. The corresponding kinetic parameters for the proposed models have been calculateden_US
dc.description.sponsorshipThe authors gratefully acknowledge financial support from the Spanish Ministerio de Economía y Competitividad (MINECO) through the project CTM2011-28352. M. Martín Martínez and A. Arévalo Bastante acknowledges the Spanish Ministerio de Ciencia e nnovación (MICINN) and the European Social Fund for her research granten_US
dc.format.extent26 pag.en
dc.format.mimetypeapplication/pdfen
dc.language.isoengen
dc.publisherAmerican Chemical Societyen_US
dc.relation.ispartofIndustrial and Engineering Chemistry Researchen_US
dc.rights© 2015 American Chemical Societyen_US
dc.subject.otherCatalyst deactivationen_US
dc.subject.otherCarbonen_US
dc.subject.otherActivated carbonen_US
dc.titleKinetic study of the hydrodechlorination of chloromethanes with activated-carbon-supported metallic catalystsen_US
dc.typearticleen
dc.subject.ecienciaQuímicaes_ES
dc.date.embargoend2016-02-26
dc.relation.publisherversionhttp://dx.doi.org/10.1021/ie5042484es_ES
dc.identifier.doi10.1021/ie5042484es_ES
dc.identifier.publicationfirstpage2023es_ES
dc.identifier.publicationissue7es_ES
dc.identifier.publicationlastpage2029es_ES
dc.identifier.publicationvolume54es_ES
dc.relation.projectIDGobierno de España. CTM2011-28352es_ES
dc.type.versioninfo:eu-repo/semantics/acceptedVersionen
dc.rights.accessRightsopenAccessen
dc.authorUAMBedia García-Matamoros, Jorge (262140)
dc.facultadUAMFacultad de Ciencias


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