dc.contributor.author | López, Laura | |
dc.contributor.author | Rivas Siota, Sandra | |
dc.contributor.author | Moure Varela, Andrés | |
dc.contributor.author | Vila, Carlos | |
dc.contributor.author | Parajo Liñares, Juan Carlos | |
dc.date.accessioned | 2021-03-01T11:44:58Z | |
dc.date.available | 2021-03-01T11:44:58Z | |
dc.date.issued | 2020-10-14 | |
dc.identifier.citation | Agronomy, 10(10): 1568 (2020) | spa |
dc.identifier.issn | 20734395 | |
dc.identifier.uri | http://hdl.handle.net/11093/1810 | |
dc.description.abstract | Hazelnut shells are an important waste from the hazelnut processing industry that could be valorized in a multi-product biorefinery. Individual or combined pretreatments may be integrated in processes enabling the integral fractionation of biomass. In this study, fractionation methods based on alkaline, alkaline-organosolv, organosolv, or acid-catalyzed organosolv treatments were applied to raw or autohydrolyzed hazelnut shells. A comparative analysis of results confirmed that the highest lignin removal was achieved with the acid-catalyzed organosolv delignification, which also allowed limited cellulose losses. When this treatment was applied to raw hazelnut shells, 65.3% of the lignin was removed, valuable hemicellulose-derived products were obtained, and the cellulose content of the processed solids increased up to 54%. Autohydrolysis of hazelnut shells resulted in the partial solubilization of hemicelluloses (mainly in the form of soluble oligosaccharides). Consecutive stages of autohydrolysis and acid-catalyzed organosolv delignification resulted in 47.9% lignin removal, yielding solids of increased cellulose content (55.4%) and very low content of residual hemicelluloses. The suitability of selected delignified and autohydrolyzed-delignified hazelnut shells as substrates for enzymatic hydrolysis was assessed in additional experiments. The most susceptible substrates (from acid-catalyzed organosolv treatments) reached 74.2% cellulose conversion into glucose, with a concentration of 28.52 g glucose/L. | spa |
dc.language.iso | eng | spa |
dc.publisher | Agronomy | spa |
dc.rights | Creative Commons Attribution
(CC BY) license | |
dc.rights.uri | http://creativecommons.org/licenses/by/4.0/ | |
dc.title | Development of pretreatment strategies for the fractionation of hazelnut shells in the scope of biorefinery | spa |
dc.type | article | spa |
dc.rights.accessRights | openAccess | spa |
dc.identifier.doi | 10.3390/agronomy10101568 | |
dc.identifier.editor | https://www.mdpi.com/2073-4395/10/10/1568 | spa |
dc.publisher.departamento | Enxeñaría química | spa |
dc.publisher.grupoinvestigacion | Enxeñería Química | spa |
dc.subject.unesco | 3303.03 Procesos Químicos | spa |
dc.subject.unesco | 3310.05 Ingeniería de Procesos | spa |
dc.subject.unesco | 3309.12 Aditivos Alimentarios | spa |
dc.date.updated | 2021-03-01T08:17:10Z | |
dc.computerCitation | pub_title=Agronomy|volume=10|journal_number=10|start_pag=1568|end_pag= | spa |