Recovery of pentoses-containing olive stones for their conversion into furfural in the presence of solid acid catalysts

dc.centroFacultad de Cienciases_ES
dc.contributor.authorFúnez Núñez, Inmaculada
dc.contributor.authorGarcía-Sancho, Cristina
dc.contributor.authorCecilia-Buenestado, Juan Antonio
dc.contributor.authorMoreno-Tost, Ramón
dc.contributor.authorSerrano Cantador, Luis
dc.contributor.authorMaireles-Torres, Pedro Jesús
dc.date.accessioned2022-09-16T12:01:41Z
dc.date.available2022-09-16T12:01:41Z
dc.date.issued2020-06-24
dc.departamentoQuímica Inorgánica, Cristalografía y Mineralografía
dc.description.abstractOlive stones were employed as feedstock for furfural production in two stages: 1) autohydrolysis of hemicellulosic fraction to recover their pentoses, mainly xylose, and 2) subsequent dehydration of pentoses into furfural. Autohydrolysis step was optimized by using different experimental conditions (temperature: 160-200 ºC and time: 30-75 min), giving rise to liquors with different xylose concentrations, since hydrolysis was incomplete in some cases. The combined use of a commercial γ-Al2O3 and CaCl2 led to total hydrolysis of non-hydrolyzed pentosans after autohydrolysis step, and the subsequent dehydration of pentoses into furfural. The maximum values of furfural yield and efficiency were 23 and 96%, respectively, after only 60 minutes at 150 ºC by using liquor obtained by autohydrolysis at 180 ºC and 30 min (L5.1) as source of pentoses. This liquor, L5.1, provided better catalytic results than other liquors which had shown higher xylose concentration after autohydrolysis, probably due to these latter also exhibited a higher concentration of organic acids; thus, the presence of organic acids such as acetic and lactic acid could promote side undesired reactions leading to lower furfural yields. Finally, γ-Al2O3 was more effective for furfural production under these experimental conditions than other solid acid catalysts, such as mesoporous Nb2O5, Nb-doped SBA-15 and Zr-doped HMS silicas, probably due to alumina has a higher density of acid sites.es_ES
dc.description.sponsorshipSpanish Ministry of Economy and Competitiveness (RTI2018-94918-B-C44 project), Junta de Andalucía (RNM-1565), FEDER (European Union) funds (UMA18-FEDERJA-171) and Malaga University. C.G.S. and J.A.C. thank to FEDER funds and Malaga University respectively for financial support. L.S.C. gratefully acknowledges support from Spanish MINECO via the concession of a Ramon y Cajal contract (RYC-2015-17109).es_ES
dc.identifier.doi10.1016/j.psep.2020.06.033
dc.identifier.urihttps://hdl.handle.net/10630/25019
dc.language.isoenges_ES
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internacional*
dc.rights.accessRightsopen accesses_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectCatálisises_ES
dc.subjectPentosases_ES
dc.subject.otherLignocellulosic biomasses_ES
dc.subject.otherHemicellulosic liquorses_ES
dc.subject.otherOlive stoneses_ES
dc.subject.otherXylose dehydrationes_ES
dc.subject.otherFurfurales_ES
dc.subject.otherSolid acid catalystses_ES
dc.titleRecovery of pentoses-containing olive stones for their conversion into furfural in the presence of solid acid catalystses_ES
dc.typejournal articlees_ES
dc.type.hasVersionSMUR
dspace.entity.typePublication
relation.isAuthorOfPublication1795b56c-12cc-4e3c-944b-d9597623a70e
relation.isAuthorOfPublicationd40b59f8-1061-40c5-a3cc-bb854403414f
relation.isAuthorOfPublicationff30d4ca-4926-4d6d-976a-63e292d0e11c
relation.isAuthorOfPublication19cb0245-0a2c-4dda-8493-d1d7ed820216
relation.isAuthorOfPublication.latestForDiscovery1795b56c-12cc-4e3c-944b-d9597623a70e

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