Catalytic upgrading of lignin-derived bio-oils over ion-exchanges H-ZSM-5 and H-Beta zeolites

dc.contributor.authorAvila, M.I.
dc.contributor.authorAlonso-Doncel, M.M.
dc.contributor.authorBriones, L.
dc.contributor.authorGómez-Pozuelo, G.
dc.contributor.authorEscola, J. M.
dc.contributor.authorSerrano, D.P.
dc.contributor.authorPeral, A.
dc.contributor.authorBotas, J. A.
dc.date.accessioned2023-12-19T10:31:49Z
dc.date.available2023-12-19T10:31:49Z
dc.date.issued2023-10-20
dc.descriptionThe authors gratefully acknowledge the financial support from the Science and Innovation Ministry and the Spanish Agency of Research through project ADBIOCAP (PID2020-114740RB-C22/AEI/10.13039/ 501100011033).es
dc.description.abstractH-ZSM-5 and H-Beta zeolites ion-exchanged with alkali (Na+ and K+) and alkaline-earth (Mg2+) metals have been explored for the catalytic fast pyrolysis of lignin. Incorporating these metals led to a significant change in the acidic properties of the parent zeolites turning into mostly Lewis-type acidity. Catalytic fast pyrolysis experiments of lignin were performed in a fixed bed reactor with ex-situ configuration operating at 550 ◦C (thermal zone) and 450 ◦C (catalytic zone), atmospheric pressure and under a nitrogen flow. Moreover, two catalysts to lignin mass ratios (C/L = 0.2 and 0.4) were studied. Compared with non-catalytic tests, the use of parent zeolites caused a decrease in the bio-oil* (water-free basis) yield due to enhanced production of gases, water, and the coke deposition on the catalyst. In addition, the quality of bio-oil* was improved since it presents a lower oxygen content regarding the thermal test. H-Beta zeolite showed a higher deoxygenation degree than H-ZSM-5, but the latter exhibited a higher share of light components in the bio-oil* that can be detected by GC-MS analyses. Both catalysts promoted the production of light oxygenates, aromatics, and oxygenated aromatics. Regarding the effect of the incorporation of metals, oxygenated aromatic compounds were the predominant family in the biooil* obtained with all ion-exchanged zeolites. Likewise, significant differences were observed among the catalysts regarding the main components of this family (alkylphenols, guaiacols, syringols, catechols, and methoxybenzenes), achieving guaiacols concentrations in bio-oil* near to 24 wt.% for NaH-ZSM-5 and KH-ZSM-5 catalysts, and alkylphenols concentrations close to 16 wt.% for MgH-Beta and KH-Beta zeolites.es
dc.identifier.citationCatal. Today 427 (2024) 114419es
dc.identifier.doi10.1016/j.cattod.2023.114419es
dc.identifier.issn0920-5861
dc.identifier.urihttps://hdl.handle.net/10115/27449
dc.language.isoenges
dc.publisherElsevieres
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectlignin pyrolysises
dc.subjectH-ZSM-5es
dc.subjectH-Betaes
dc.subjectIon-exchanged zeoliteses
dc.subjectoxygenated aromaticses
dc.titleCatalytic upgrading of lignin-derived bio-oils over ion-exchanges H-ZSM-5 and H-Beta zeoliteses
dc.typeinfo:eu-repo/semantics/articlees

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