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dc.contributor.authorValle Pascual, Beatriz
dc.contributor.authorGarcía Gómez, Naiara
dc.contributor.authorRemiro Eguskiza, Aingeru
dc.contributor.authorGayubo Cazorla, Ana Guadalupe ORCID
dc.contributor.authorBilbao Elorriaga, Javier
dc.date.accessioned2020-10-02T17:48:38Z
dc.date.available2020-10-02T17:48:38Z
dc.date.issued2019-07-19
dc.identifier.citationFuel Processing Technology 195 : (2019) // art. id: 106142 // https://doi.org/10.1016/j.fuproc.2019.106142es_ES
dc.identifier.issn0378-3820
dc.identifier.urihttp://hdl.handle.net/10810/46399
dc.description.abstractThis study deals with a continuous process on a calcined dolomite operating at atmospheric pressure and by cofeeding water for cost-effective upgrading of raw bio-oil at 400 °C and 500 °C. The distribution of carbon in the feed to the product fractions (gas and upgraded bio-oil) and to the dolomite (as CO2 captured and coke) was investigated with time on stream, as well as the evolution of the gas and the upgraded bio-oil composition. Acids and high-molecular weight phenols were completely removed from the raw bio-oil for 0.5 h time on stream, with the upgraded bio-oil being mainly composed of ketones (acetone, 2-butanone and cyclopentanones). Chromatographic analyses of the reaction products were combined with analysis of the dolomite characteristics by thermogravimetry and X-ray diffraction. The results are explained on the basis of possible reaction mechanisms on the dolomite basic sites (CaO, Ca(OH)2 and MgO) and the extent of dolomite carbonation with adsorbed CO2. Composition of the upgraded bio-oil makes it suitable for further catalytic valorization for obtaining fuels and chemicals, such as H2 (by steam reforming) and aromatic hydrocarbons (by dual-stage hydrogenation- cracking processes).es_ES
dc.description.sponsorshipThis work was carried out with the financial support of the Department of Education Universities and Investigation of the Basque Government (IT2018-19), the Ministry of Economy and Competitiveness of the Spanish Government jointly with European Regional Development Funds (AEI/FEDER, UE) (Project CTQ2015- 68883-R), the European Commission (HORIZON H2020-MSCA-RISE- 2018, Contract No. 823745), and PhD grant (BES-2016-078132) for N. García-Gómez.es_ES
dc.language.isoenges_ES
dc.publisherElsevier B.V.es_ES
dc.relationinfo:eu-repo/grantAgreement/EC/H2020/823745es_ES
dc.relationinfo:eu-repo/grantAgreement/MINECO/CTQ2015- 68883-Res_ES
dc.rightsinfo:eu-repo/semantics/openAccesses_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
dc.subjectraw bio-oiles_ES
dc.subjectupgradinges_ES
dc.subjectbasic catalystes_ES
dc.subjectdolomitees_ES
dc.subjectketonizationes_ES
dc.titleCost-effective upgrading of biomass pyrolysis oil using activated dolomite as a basic catalystes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.holder© 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 licensees_ES
dc.relation.publisherversionhttps://www.sciencedirect.com/science/article/pii/S0378382019310501es_ES
dc.identifier.doi10.1016/j.fuproc.2019.106142
dc.contributor.funderEuropean Commission
dc.departamentoesIngeniería químicaes_ES
dc.departamentoeuIngeniaritza kimikoaes_ES


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© 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 license
Except where otherwise noted, this item's license is described as © 2019. This manuscript version is made available under the CC-BY-NC-ND 4.0 license