Publication: Highly active Fe-Co-Zn/K-Al2O3 catalysts for CO2 hydrogenation to light olefins
| dc.citedby | 23 | |
| dc.contributor.author | Witoon T. | en_US |
| dc.contributor.author | Chaipraditgul N. | en_US |
| dc.contributor.author | Numpilai T. | en_US |
| dc.contributor.author | Lapkeatseree V. | en_US |
| dc.contributor.author | Ayodele B.V. | en_US |
| dc.contributor.author | Cheng C.K. | en_US |
| dc.contributor.author | Siri-Nguan N. | en_US |
| dc.contributor.author | Sornchamni T. | en_US |
| dc.contributor.author | Limtrakul J. | en_US |
| dc.contributor.authorid | 23487511100 | en_US |
| dc.contributor.authorid | 57219253139 | en_US |
| dc.contributor.authorid | 56896137000 | en_US |
| dc.contributor.authorid | 57221501569 | en_US |
| dc.contributor.authorid | 56862160400 | en_US |
| dc.contributor.authorid | 57204938666 | en_US |
| dc.contributor.authorid | 55770826900 | en_US |
| dc.contributor.authorid | 6507994399 | en_US |
| dc.contributor.authorid | 7003474789 | en_US |
| dc.date.accessioned | 2023-05-29T09:08:27Z | |
| dc.date.available | 2023-05-29T09:08:27Z | |
| dc.date.issued | 2021 | |
| dc.description | Aluminum compounds; Carbides; Carbon dioxide; Catalyst activity; Hydrogenation; Iron oxides; Light olefins; Paraffins; Zinc; Active site; CO2 hydrogenation; Function of time; Iron carbides; Light olefins yield; Number of active sites; Optimum operating conditions; Zn content; Zinc compounds | en_US |
| dc.description.abstract | CO2 hydrogenation to light olefins over Fe-Co-Zn/K-Al2O3 catalysts with different Zn loading contents (0�1.74 wt%) is studied. The addition of Zn improves the dispersion and the reducibility of iron oxides. The amount of CO adsorbed of the catalysts showed a volcanic trend as a function of Zn content with its maximum of 2.42 ?mol g?1 at 0.58 wt% Zn, suggesting an increase of number of active sites. The 0.58 wt% Zn-promoted Fe-Co/K-Al2O3 catalyst shows superior activity for light olefins yield (19.9%) under the optimum operating conditions of 340 �C, 25 bar, 9,000 mL gcat?1 h?1 and H2 to CO2 ratio = 4. A gradual decrease in olefin to paraffin ratio with an almost constant CO2 conversion as a function of time-on-stream is observed, which is related to a continuous increase of iron carbide content, indicating that the iron carbide can be acted as the active site for paraffins production. � 2021 Elsevier Ltd | en_US |
| dc.description.nature | Final | en_US |
| dc.identifier.ArtNo | 116428 | |
| dc.identifier.doi | 10.1016/j.ces.2020.116428 | |
| dc.identifier.scopus | 2-s2.0-85099283251 | |
| dc.identifier.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85099283251&doi=10.1016%2fj.ces.2020.116428&partnerID=40&md5=1f38249afff07679d3af8e1d421bb79b | |
| dc.identifier.uri | https://irepository.uniten.edu.my/handle/123456789/26266 | |
| dc.identifier.volume | 233 | |
| dc.publisher | Elsevier Ltd | en_US |
| dc.source | Scopus | |
| dc.sourcetitle | Chemical Engineering Science | |
| dc.title | Highly active Fe-Co-Zn/K-Al2O3 catalysts for CO2 hydrogenation to light olefins | en_US |
| dc.type | Article | en_US |
| dspace.entity.type | Publication |