Production of phenolic compounds from argan shell waste by reductive catalytic fractionation
For efficient utilization of lignocellulosic biomass components, reductive catalytic fractionation appears as a promising biorefinery strategy. In this work, this concept of biomass valorization was used to study the potential of an unexplored feedstock, argan shells. This material was processed in...
| Autores: | , , , , , |
|---|---|
| Tipo de recurso: | artículo |
| Estado: | Versión publicada |
| Fecha de publicación: | 2023 |
| País: | España |
| Institución: | Universidad San Jorge (USJ) |
| Repositorio: | Academica-e. Repositorio Institucional de la Universidad Pública de Navarra |
| OAI Identifier: | oai:academica-e.unavarra.es:2454/48232 |
| Acceso en línea: | https://hdl.handle.net/2454/48232 |
| Access Level: | acceso abierto |
| Palabra clave: | Agricultural waste Argan shells Hydrogenolysis Native lignin Reductive catalytic fractionation |
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Production of phenolic compounds from argan shell waste by reductive catalytic fractionationAfailal, ZainabGil-Lalaguna, NoemíHøj, MartinCornejo Ibergallartu, AlfonsoSánchez, José LuisJensen, Anker DegnAgricultural wasteArgan shellsHydrogenolysisNative ligninReductive catalytic fractionationFor efficient utilization of lignocellulosic biomass components, reductive catalytic fractionation appears as a promising biorefinery strategy. In this work, this concept of biomass valorization was used to study the potential of an unexplored feedstock, argan shells. This material was processed in a non-catalytic route and over a Pd/C catalyst in two different reaction media. The effects of the treatment temperature (250, 275, and 300 °C), as well as the catalyst loading (catalyst/argan shells mass ratio of 0.05 and 0.1 g/g), were also studied. The main product (lignin-derived oil) was thoroughly characterized using GC/MS/FID, SEC, and NMR. The highest monomer yields of 48-49 wt% based on the lignin content were obtained for n-butanol/water reaction medium at 300 °C using a Pd/C catalyst load of 0.1 g/g and for methanol reaction medium at 275 °C and 0.05 g/g. Significantly lower monomeric phenol yields were obtained in the non-catalytic route (4-19 wt% for n-butanol/water and 9-16 wt% for methanol). The main phenolic monomers in the catalytic pathway were 4-n-propanolguaiacol, 4-n-propanolsyringol, and 4-alkyl guaiacols and syringols, with some differences in the selectivities from one solvent to another.The authors express gratitude to Agencia Estatal de Investigación in Spain (Project PID2020-114936RB-I00), Aragón Government (Research Group Ref. T22_23R), and Navarra Government (Project 'PC177-178 Reducenano 2.0') for providing frame support for this work. Open Access funding provided thanks to the CRUE-CSIC agreement with Springer Nature.SpringerCienciasZientziakInstitute for Advanced Materials and Mathematics - INAMAT22023info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionapplication/pdfapplication/mswordhttps://hdl.handle.net/2454/48232reponame:Academica-e. Repositorio Institucional de la Universidad Pública de Navarrainstname:Universidad San Jorge (USJ)Inglésinfo:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica y Técnica y de Innovación 2017-2020/PID2020-114936RB-I00info:eu-repo/grantAgreement/Gobierno de Navarra//PC177-178This article is licensed under a Creative Commons Attribution 4.0 International License.https://creativecommons.org/licenses/by/4.0/info:eu-repo/semantics/openAccessoai:academica-e.unavarra.es:2454/482322026-06-17T12:41:47Z |
| dc.title.none.fl_str_mv |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| title |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| spellingShingle |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation Afailal, Zainab Agricultural waste Argan shells Hydrogenolysis Native lignin Reductive catalytic fractionation |
| title_short |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| title_full |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| title_fullStr |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| title_full_unstemmed |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| title_sort |
Production of phenolic compounds from argan shell waste by reductive catalytic fractionation |
| dc.creator.none.fl_str_mv |
Afailal, Zainab Gil-Lalaguna, Noemí Høj, Martin Cornejo Ibergallartu, Alfonso Sánchez, José Luis Jensen, Anker Degn |
| author |
Afailal, Zainab |
| author_facet |
Afailal, Zainab Gil-Lalaguna, Noemí Høj, Martin Cornejo Ibergallartu, Alfonso Sánchez, José Luis Jensen, Anker Degn |
| author_role |
author |
| author2 |
Gil-Lalaguna, Noemí Høj, Martin Cornejo Ibergallartu, Alfonso Sánchez, José Luis Jensen, Anker Degn |
| author2_role |
author author author author author |
| dc.contributor.none.fl_str_mv |
Ciencias Zientziak Institute for Advanced Materials and Mathematics - INAMAT2 |
| dc.subject.none.fl_str_mv |
Agricultural waste Argan shells Hydrogenolysis Native lignin Reductive catalytic fractionation |
| topic |
Agricultural waste Argan shells Hydrogenolysis Native lignin Reductive catalytic fractionation |
| description |
For efficient utilization of lignocellulosic biomass components, reductive catalytic fractionation appears as a promising biorefinery strategy. In this work, this concept of biomass valorization was used to study the potential of an unexplored feedstock, argan shells. This material was processed in a non-catalytic route and over a Pd/C catalyst in two different reaction media. The effects of the treatment temperature (250, 275, and 300 °C), as well as the catalyst loading (catalyst/argan shells mass ratio of 0.05 and 0.1 g/g), were also studied. The main product (lignin-derived oil) was thoroughly characterized using GC/MS/FID, SEC, and NMR. The highest monomer yields of 48-49 wt% based on the lignin content were obtained for n-butanol/water reaction medium at 300 °C using a Pd/C catalyst load of 0.1 g/g and for methanol reaction medium at 275 °C and 0.05 g/g. Significantly lower monomeric phenol yields were obtained in the non-catalytic route (4-19 wt% for n-butanol/water and 9-16 wt% for methanol). The main phenolic monomers in the catalytic pathway were 4-n-propanolguaiacol, 4-n-propanolsyringol, and 4-alkyl guaiacols and syringols, with some differences in the selectivities from one solvent to another. |
| publishDate |
2023 |
| dc.date.none.fl_str_mv |
2023 |
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info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion |
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article |
| status_str |
publishedVersion |
| dc.identifier.none.fl_str_mv |
https://hdl.handle.net/2454/48232 |
| url |
https://hdl.handle.net/2454/48232 |
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Inglés |
| language_invalid_str_mv |
Inglés |
| dc.relation.none.fl_str_mv |
info:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica y Técnica y de Innovación 2017-2020/PID2020-114936RB-I00 info:eu-repo/grantAgreement/Gobierno de Navarra//PC177-178 |
| dc.rights.none.fl_str_mv |
This article is licensed under a Creative Commons Attribution 4.0 International License. https://creativecommons.org/licenses/by/4.0/ info:eu-repo/semantics/openAccess |
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This article is licensed under a Creative Commons Attribution 4.0 International License. https://creativecommons.org/licenses/by/4.0/ |
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openAccess |
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application/pdf application/msword |
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Springer |
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Springer |
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reponame:Academica-e. Repositorio Institucional de la Universidad Pública de Navarra instname:Universidad San Jorge (USJ) |
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Universidad San Jorge (USJ) |
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Academica-e. Repositorio Institucional de la Universidad Pública de Navarra |
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Academica-e. Repositorio Institucional de la Universidad Pública de Navarra |
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