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Co3O4-g-C3N4 catalysts for 1-octene transformation to nonanol: Structure, activity and mechanism
[Display omitted] •Composite Co3O4 and g-C3N4 for 1-octene transformation to nonanol.•Oxygen vacancy for CO adsorption and electronic transfer from g-C3N4 to Co3O4.•Promoted successive hydroformylation-hydrogenation.•High nonanol selectivity and enhanced utilization of Co active centers. Hydroformyl...
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Published in: | Fuel (Guildford) 2024-06, Vol.365, p.131192, Article 131192 |
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Main Authors: | , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites |
Online Access: | Get full text |
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Summary: | [Display omitted]
•Composite Co3O4 and g-C3N4 for 1-octene transformation to nonanol.•Oxygen vacancy for CO adsorption and electronic transfer from g-C3N4 to Co3O4.•Promoted successive hydroformylation-hydrogenation.•High nonanol selectivity and enhanced utilization of Co active centers.
Hydroformylation reactions of olefins are one of the important applied transformations in the syngas industry, mainly using homogeneous noble catalysts. Here the composite of zeolitic imidazolate framework (ZIF-67) derived Co3O4 with g-C3N4 for catalyzing 1-octene transformation under pressured syngas has been investigated. Using 5 wt% Co3O4-g-C3N4 in the reaction at 150 °C and 7 MPa for 8 h, 1-octene conversion and nonanol selectivity reached 99.9 % and 77.8 %, respectively. At 110 °C, a nonanal selectivity of 90 % was achieved. TEM, CO–/H2-TPD, XPS, in situ XRD and in situ DRIFTS characterization indicated that as-synthesized Co3O4 precursor showed dominantly exposed (220) and (311) crystal planes. The oxygen vacancy proportion on 5 %Co3O4-g-C3N4 reached 56 %, which enhanced the CO adsorption, in addition to Co3O4 dispersion on the g-C3N4 surface for raising turnover frequency. Electron transfer on the Co3O4-g-C3N4 interfaces promoted the reduction of Co3O4 to active Co. The successive hydroformylation-hydrogenation pathway was discussed for the promoted production of nonanol. |
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ISSN: | 0016-2361 |
DOI: | 10.1016/j.fuel.2024.131192 |