Designing continuous flow reaction of xylan hydrolysis for xylooligosaccharides production in packed-bed reactors using xylanase immobilized on methacrylic polymer-based supports
| dc.contributor.author | Romero Fernández, María | |
| dc.contributor.author | Moreno Pérez, Sonia | |
| dc.contributor.author | Orrego, Alejandro H. | |
| dc.contributor.author | Martins de Oliveira, Sandro | |
| dc.contributor.author | Santamaría, Ramón I. | |
| dc.contributor.author | Díaz, Margarita | |
| dc.contributor.author | Guisan, José M. | |
| dc.contributor.author | Rocha Martín, Javier | |
| dc.date.accessioned | 2019-07-12T18:55:50Z | |
| dc.date.available | 2019-07-12T18:55:50Z | |
| dc.date.issued | 2018 | |
| dc.description.abstract | The present study focuses on the development and optimization of a packed-bed reactor (PBR) for continuous production of xylooligosaccharides (XOS) from xylan. For this purpose, three different methacrylic polymer-based supports (Relizyme R403/S, Purolite P8204F and Purolite P8215F) activated with glyoxyl groups were morphologically characterized and screened for the multipoint covalent immobilization of a xylanase. Based on its physical and mechanical properties, maximum protein loading and thermal stability, Relizyme R403/S was selected to set up a PRB for continuous production of XOS from corncob xylan. The specific productivity for XOS at 10 mL/min flow rate was 3277 gXOS genzyme−1 h−1 with a PBR. This PBR conserved >90% of its initial activity after 120 h of continuous operation. | spa |
| dc.description.filiation | UEM | spa |
| dc.description.impact | 6.669 JCR (2018) Q1, 1/13 Agricultural Engineering, 13/162 Biotechnology & Applied Microbiology, 13/103 Energy & Fuels | spa |
| dc.description.impact | 2.157 SJR (2018) Q1, 13/188 Bioengineering, 14/352 Renewable Energy, Sustainability and the Environment, 2/200 Environmental Engineering, 2/129 Waste Management and Disposal, 134/2844 Medicine (miscellaneous) | spa |
| dc.description.impact | No data IDR 2018 | spa |
| dc.description.sponsorship | Sin financiación | spa |
| dc.identifier.citation | Romero-Fernández, M., Moreno-Perez, S., H. Orrego, A., de Oliveira, S., I. Santamaría, R., Díaz, M., … & Rocha-Martin, J. (2018). Designing continuous flow reaction of xylan hydrolysis for xylooligosaccharides production in packed-bed reactors using xylanase immobilized on methacrylic polymer-based supports. Bioresource Technology, 266, 249–258. https://doi.org/10.1016/j.biortech.2018.06.070 | spa |
| dc.identifier.doi | 10.1016/j.biortech.2018.06.070 | |
| dc.identifier.issn | 0960-8524 | |
| dc.identifier.issn | 1873-2976 | |
| dc.identifier.uri | http://hdl.handle.net/11268/8127 | |
| dc.language.iso | eng | spa |
| dc.peerreviewed | Si | spa |
| dc.rights.accessRights | restricted access | spa |
| dc.subject.uem | Enzimas | spa |
| dc.subject.uem | Biología molecular | spa |
| dc.subject.unesco | Biología molecular | spa |
| dc.subject.unesco | Enzima | spa |
| dc.title | Designing continuous flow reaction of xylan hydrolysis for xylooligosaccharides production in packed-bed reactors using xylanase immobilized on methacrylic polymer-based supports | spa |
| dc.type | journal article | spa |
| dspace.entity.type | Publication | |
| relation.isAuthorOfPublication | 1234b64c-5ae3-4c75-a8a2-7befb13d9a6b | |
| relation.isAuthorOfPublication.latestForDiscovery | 1234b64c-5ae3-4c75-a8a2-7befb13d9a6b |

