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Industrial crude bioethanol dehydration to ethylene: doping zsm-5 to enhance selectivity and stability
dc.contributor.author | Quiroga E | |
dc.contributor.author | García N | |
dc.contributor.author | Cifuentes B | |
dc.contributor.author | Cogua R | |
dc.contributor.author | Becerra J | |
dc.contributor.author | Berenguer J.M | |
dc.contributor.author | Cobo M. | |
dc.date.accessioned | 2024-11-01T14:38:44Z | |
dc.date.available | 2024-11-01T14:38:44Z | |
dc.date.issued | 2024 | |
dc.identifier.issn | 22133437 | |
dc.identifier.other | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85183743214&doi=10.1016%2fj.jece.2023.111803&partnerID=40&md5=066228b556ffdca16fca83a5ea9d388e | |
dc.identifier.uri | http://hdl.handle.net/10818/62239 | |
dc.description.abstract | Although the conversion of bioethanol into light olefins is one of the most studied processes in biorefinery schemes, there is a need to develop materials more capable of operating at industrial conditions (WHSV > 20 h−1 crude bioethanol feed). Hence, in this study, we dehydrated crude bioethanol samples derived from sugarcane fermentation to produce ethylene over a series of H-ZSM-5 zeolites. Among them, H-ZSM-5 with different Si/Al ratios (26, 280, and 371) and doped with Ce and Cu were tested on the catalytic activity and stability. Accordingly, a 26 Si/Al ratio showed full conversion and ethylene selectivity at 300 °C with a WHSV of 30.2 h−1. When doping the zeolites, a decrease in relative crystallinity and a higher amount of acid sites were observed, which affected the interaction with reactants. This interaction was deeply analyzed by the in-situ DRIFTS, which showed that ethanol adsorption is lower for doped zeolites, but the desorption rate is higher, showing higher stability over longer reaction times. Therefore, the H-ZSM-5 with a Si/Al ratio of 26 and doped with Ce maintained its activity and improved its selectivity over 140 h under more drastic conditions of WHSV (42.3 h−1). These results elucidate that Ce-doped H-ZSM-5 zeolites can improve stability and represent a starting point for large-scale crude bioethanol conversion. © 2024 Elsevier Ltd | en |
dc.format | application/pdf | es_CO |
dc.language.iso | eng | es_CO |
dc.publisher | Journal of Environmental Chemical Engineering | es_CO |
dc.relation.ispartofseries | Journal of Environmental Chemical Engineering Vol. 12 N° 1 | |
dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 International | * |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
dc.source | Universidad de La Sabana | es_CO |
dc.source | Intellectum Repositorio Universidad de La Sabana | es_CO |
dc.subject.other | Bioethanol | en |
dc.subject.other | Catalyst activity | en |
dc.subject.other | Crystallinity | en |
dc.subject.other | Ethanol | en |
dc.subject.other | Refining | en |
dc.subject.other | Silicon | en |
dc.subject.other | Stability | en |
dc.subject.other | Zeolites | en |
dc.subject.other | Bio-ethanols | en |
dc.subject.other | Bio-ethylene | en |
dc.subject.other | Bioethylene production | en |
dc.title | Industrial crude bioethanol dehydration to ethylene: doping zsm-5 to enhance selectivity and stability | en |
dc.type | journal article | es_CO |
dc.type.hasVersion | publishedVersion | es_CO |
dc.rights.accessRights | openAccess | es_CO |
dc.identifier.doi | 10.1016/j.jece.2023.111803 |
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Facultad de Ingeniería [506]