Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural
The production of furfural from renewable sources, such as lignocellulosic biomass, has gained great interest within the concept of biorefineries. In lignocellulosic materials, xylose is the most abundant pentose, which forms the hemicellulosic part. One of the key steps in the production of furfura...
| Autores: | , , , |
|---|---|
| Tipo de documento: | artigo |
| Estado: | Versión aceptada para publicación |
| Data de publicação: | 2020 |
| País: | España |
| Recursos: | Universidad de Jaén |
| Repositório: | RUJA. Repositorio Institucional de la Producción Científica de la Universidad de Jaén |
| OAI Identifier: | oai:ruja.ujaen.es:10953/7536 |
| Acesso em linha: | https://doi.org/10.3390/MOLECULES25163574 https://hdl.handle.net/10953/7536 |
| Access Level: | Acceso aberto |
| Palavra-chave: | lignocellulosic material xylose furfural iron chloride microwave reactor biorefinery 66.011.47 |
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Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to FurfuralPadilla-Rascón, C.Romero-García, J. M.Ruiz, E.Castro, E.lignocellulosic materialxylosefurfuraliron chloridemicrowave reactorbiorefinery66.011.47The production of furfural from renewable sources, such as lignocellulosic biomass, has gained great interest within the concept of biorefineries. In lignocellulosic materials, xylose is the most abundant pentose, which forms the hemicellulosic part. One of the key steps in the production of furfural from biomass is the dehydration reaction of the pentoses. The objective of this work was to assess the conditions at which the concentration of furfural is maximized from a synthetic, monophasic and homogeneous xylose medium. The experiments were carried out in a microwave reactor. FeCl3 in different proportions and sulfuric acid were used as catalysts. A two-level, three-factor experimental design was developed for this purpose. Results were further analysed through a second experimental design and optimization was performed by Response Surface Methodology. The best operational conditions for the highest furfural yield (57%) turned to be 210 ˚C, 0.5 min and 0.05 M FeCl3.The authors want to acknowledge the financial support from Agencia Estatal de Investigación (MICINN, Spain) and Fondo Europeo de Desarrollo Regional, reference project ENE2017-85819-C2-1-R. C.P.-R. was supported by Universidad de Jaén (research grant R5/04/2017).MDPI202620262020info:eu-repo/semantics/articleinfo:eu-repo/semantics/acceptedVersionapplication/pdfhttps://doi.org/10.3390/MOLECULES25163574https://hdl.handle.net/10953/7536reponame:RUJA. Repositorio Institucional de la Producción Científica de la Universidad de Jaéninstname:Universidad de JaénInglésMoleculesAttribution-NonCommercial-NoDerivs 3.0 Spainhttp://creativecommons.org/licenses/by-nc-nd/3.0/es/info:eu-repo/semantics/openAccessoai:ruja.ujaen.es:10953/75362026-06-24T12:41:07Z |
| dc.title.none.fl_str_mv |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| title |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| spellingShingle |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural Padilla-Rascón, C. lignocellulosic material xylose furfural iron chloride microwave reactor biorefinery 66.011.47 |
| title_short |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| title_full |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| title_fullStr |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| title_full_unstemmed |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| title_sort |
Optimization with Response Surface Methodology of Microwave-Assisted Conversion of Xylose to Furfural |
| dc.creator.none.fl_str_mv |
Padilla-Rascón, C. Romero-García, J. M. Ruiz, E. Castro, E. |
| author |
Padilla-Rascón, C. |
| author_facet |
Padilla-Rascón, C. Romero-García, J. M. Ruiz, E. Castro, E. |
| author_role |
author |
| author2 |
Romero-García, J. M. Ruiz, E. Castro, E. |
| author2_role |
author author author |
| dc.subject.none.fl_str_mv |
lignocellulosic material xylose furfural iron chloride microwave reactor biorefinery 66.011.47 |
| topic |
lignocellulosic material xylose furfural iron chloride microwave reactor biorefinery 66.011.47 |
| description |
The production of furfural from renewable sources, such as lignocellulosic biomass, has gained great interest within the concept of biorefineries. In lignocellulosic materials, xylose is the most abundant pentose, which forms the hemicellulosic part. One of the key steps in the production of furfural from biomass is the dehydration reaction of the pentoses. The objective of this work was to assess the conditions at which the concentration of furfural is maximized from a synthetic, monophasic and homogeneous xylose medium. The experiments were carried out in a microwave reactor. FeCl3 in different proportions and sulfuric acid were used as catalysts. A two-level, three-factor experimental design was developed for this purpose. Results were further analysed through a second experimental design and optimization was performed by Response Surface Methodology. The best operational conditions for the highest furfural yield (57%) turned to be 210 ˚C, 0.5 min and 0.05 M FeCl3. |
| publishDate |
2020 |
| dc.date.none.fl_str_mv |
2020 2026 2026 |
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info:eu-repo/semantics/article info:eu-repo/semantics/acceptedVersion |
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article |
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acceptedVersion |
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https://doi.org/10.3390/MOLECULES25163574 https://hdl.handle.net/10953/7536 |
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https://doi.org/10.3390/MOLECULES25163574 https://hdl.handle.net/10953/7536 |
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Inglés |
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Inglés |
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Molecules |
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Attribution-NonCommercial-NoDerivs 3.0 Spain http://creativecommons.org/licenses/by-nc-nd/3.0/es/ info:eu-repo/semantics/openAccess |
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Attribution-NonCommercial-NoDerivs 3.0 Spain http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
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openAccess |
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MDPI |
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MDPI |
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