Interface-engineered inverse ZnO/Cu for low-temperature CO2 hydrogenation to methanol

•Highly porous CuO with specific surface area up to 120 m2/g is prepared as intermediate to produce porous Cu substance.•Nearly 8.3 % CO2 conversion and above 99% methanol selectivity is achieved in the 50 wt.% ZnO/Cu inverse catalyst.•The STY of methanol presents a particular volcanic curve related...

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Veröffentlicht in:Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2024-11, Vol.499, p.155826, Article 155826
Hauptverfasser: Shu, Yuan, Zhang, Zequn, Wang, Panpan, Ma, Ziming, Bi, Shuxian, Shi, Meiyu, Zhang, Pengfei
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Sprache:eng
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Zusammenfassung:•Highly porous CuO with specific surface area up to 120 m2/g is prepared as intermediate to produce porous Cu substance.•Nearly 8.3 % CO2 conversion and above 99% methanol selectivity is achieved in the 50 wt.% ZnO/Cu inverse catalyst.•The STY of methanol presents a particular volcanic curve related to Cu-ZnO interface.•ZnO vacancy concentration formed by Cu-ZnO SMSI greatly affects the selectivity of CO2 hydrogenation into methanol. Herein, via a mechanical-assisted NaCl template method, inverse ZnO/Cu catalysts with controllable ZnO loading weights from 5 to 100 wt% are successfully designed. During CO2 hydrogenation, we find that the space–time yield (STY) of methanol is greatly affected by the ZnO loading weights, and presents a particular volcanic curve related to the nominal loading weights of ZnO. The data of HRTEM and EDS mappings reveals the formation of ZnO-Cu strong metal-supporting interaction (SMSI) after H2 reduction. Meanwhile, the chemistry probe studies discover that the concentration of surface-adsorbed CO2 and H2 depended on the ZnO loading weight. On these grounds, the 50% ZnO loading weight is suggested as the optimized value, where both the surface-adsorbed CO2 and H2 species reached equilibrium. In addition, we also observe that the oxygen vacancy concentration of ZnO fluctuated with the reaction temperatures by Quasi-In-situ XPS, further leading to a change in the CO2 hydrogenation reaction path.
ISSN:1385-8947
DOI:10.1016/j.cej.2024.155826