dc.contributor.author | Santamaría Moreno, Laura ![ORCID](/themes/Mirage2//images/orcid_16x16.png) | |
dc.contributor.author | Artetxe Uria, Maite | |
dc.contributor.author | López Zabalbeitia, Gartzen ![ORCID](/themes/Mirage2//images/orcid_16x16.png) | |
dc.contributor.author | Cortázar Dueñas, María ![ORCID](/themes/Mirage2//images/orcid_16x16.png) | |
dc.contributor.author | Amutio Izaguirre, Maider | |
dc.contributor.author | Bilbao Elorriaga, Javier | |
dc.contributor.author | Olazar Aurrecoechea, Martin ![ORCID](/themes/Mirage2//images/orcid_16x16.png) | |
dc.date.accessioned | 2020-10-02T16:31:16Z | |
dc.date.available | 2020-10-02T16:31:16Z | |
dc.date.issued | 2019-10-25 | |
dc.identifier.citation | Fuel Processing Technology 198 : (2020) // art. id: 106223 // https://doi.org/10.1016/j.fuproc.2019.106223 | es_ES |
dc.identifier.issn | 0378-3820 | |
dc.identifier.uri | http://hdl.handle.net/10810/46373 | |
dc.description.abstract | A Ni/Al2O3 catalyst has been modified incorporating CeO2 and MgO promoters in order to improve its performance in the steam reforming of biomass pyrolysis volatiles. Ni/Al2O3, Ni/CeO2-Al2O3 and Ni/MgO-Al2O3 catalysts have been prepared and fresh and deactivated catalysts have been characterized by N2 adsorption/ desorption, X-ray Fluorescence (XRF), Temperature Programmed Reduction (TPR), X-ray powder diffraction (XRD), Temperature Programmed Oxidation (TPO), Transmission Electron Microscopy (TEM) and a technique based on Fourier Transform Infrared Spectroscopy-Temperature Programmed Oxidation (FTIR-TPO). The results obtained revealed a similar initial activity for the three catalysts tested (conversion higher than 98%), whereas stability has been greatly improved by incorporating CeO2 as promoter, as it enhances the gasification of coke precursors. However, Ni/MgO-Al2O3 catalyst is slightly less stable than Ni/Al2O3, presumably as a result of its lower reducibility due to the formation of MgAl2O4 spinel phase. Catalysts deactivation has been associated with coke deposition, although sintering phenomenon became also evident when the Ni/CeO2-Al2O3 catalyst was tested. The coke deposited on the catalysts does not present any specific morphology, which is evidence of its amorphous structure in the three catalysts studied. | es_ES |
dc.description.sponsorship | This work was carried out with financial support from the Ministry of Economy and Competitiveness of the Spanish Government (CTQ2016-75535-R (AEI/FEDER, UE) and CTQ-2015-69436-R (MINECO/FEDER, UE)), Ministry of Science, Innovation and Universities of the Spanish Government (RTI2018-101678-B-I00 (MCIU/AEI/FEDER, UE)), the European Union’s Horizon 2020 research and innovation programme under the Marie Skłodowska-Curie grant agreement No 823745, and the Basque Government (IT1218-19). | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | Elsevier B.V. | es_ES |
dc.relation | info:eu-repo/grantAgreement/EC/H2020/823745 | es_ES |
dc.relation | info:eu-repo/grantAgreement/MINECO/CTQ2016-75535-R | es_ES |
dc.relation | info:eu-repo/grantAgreement/MINECO/CTQ2015-69436-R | es_ES |
dc.relation | info:eu-repo/grantAgreement/MCIU/RTI2018-101678-B-I00 | es_ES |
dc.rights | info:eu-repo/semantics/openAccess | es_ES |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/3.0/es/ | |
dc.subject | hydrogen | es_ES |
dc.subject | steam reforming | es_ES |
dc.subject | biomass | es_ES |
dc.subject | nickel catalyst | es_ES |
dc.subject | promoters | es_ES |
dc.subject | ceria | es_ES |
dc.title | Effect of CeO2 and MgO promoters on the performance of a Ni/Al2O3 catalyst in the steam reforming of biomass pyrolysis volatiles | es_ES |
dc.type | info:eu-repo/semantics/article | es_ES |
dc.rights.holder | © 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 license | es_ES |
dc.relation.publisherversion | https://www.sciencedirect.com/science/article/pii/S0378382019308562 | es_ES |
dc.identifier.doi | 10.1016/j.fuproc.2019.106223 | |
dc.contributor.funder | European Commission | |
dc.departamentoes | Ingeniería química | es_ES |
dc.departamentoeu | Ingeniaritza kimikoa | es_ES |