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Influence of Defects and H(2)O on the Hydrogenation of CO(2) to Methanol over Pt Nanoparticles in UiO-67 Metal–Organic Framework

[Image: see text] In catalysts for CO(2) hydrogenation, the interface between metal nanoparticles (NPs) and the support material is of high importance for the activity and reaction selectivity. In Pt NP-containing UiO Zr-metal–organic frameworks (MOFs), key intermediates in methanol formation are ad...

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Detalles Bibliográficos
Autores principales: Gutterød, Emil Sebastian, Pulumati, Sri Harsha, Kaur, Gurpreet, Lazzarini, Andrea, Solemsli, Bjørn Gading, Gunnæs, Anette Eleonora, Ahoba-Sam, Christian, Kalyva, Maria Evangelou, Sannes, Johnny Andreas, Svelle, Stian, Skúlason, Egill, Nova, Ainara, Olsbye, Unni
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2020
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7586342/
https://www.ncbi.nlm.nih.gov/pubmed/32902970
http://dx.doi.org/10.1021/jacs.0c07153
Descripción
Sumario:[Image: see text] In catalysts for CO(2) hydrogenation, the interface between metal nanoparticles (NPs) and the support material is of high importance for the activity and reaction selectivity. In Pt NP-containing UiO Zr-metal–organic frameworks (MOFs), key intermediates in methanol formation are adsorbed at open Zr-sites at the Pt–MOF interface. In this study, we investigate the dynamic role of the Zr-node and the influence of H(2)O on the CO(2) hydrogenation reaction at 170 °C, through steady state and transient isotope exchange experiments, H(2)O cofeed measurements, and density functional theory (DFT) calculations. The study revealed that an increased number of Zr-node defects increase the formation rates to both methanol and methane. Transient experiments linked the increase to a higher number of surface intermediates for both products. Experiments involving either dehydrated or prehydrated Zr-nodes showed higher methanol and methane formation rates over the dehydrated Zr-node. Transient experiments suggested that the difference is related to competitive adsorption between methanol and water. DFT calculations and microkinetic modeling support this conclusion and give further insight into the equilibria involved in the competitive adsorption process. The calculations revealed weaker adsorption of methanol in defective or dehydrated nodes, in agreement with the larger gas phase concentration of methanol observed experimentally. The microkinetic model shows that [Zr(2)(μ-O)(2)](4+) and [Zr(2)(μ–OH)(μ-O)(OH)(H(2)O)](4+) are the main surface species when the concentration of water is lower than the number of defect sites. Lastly, although addition of water was found to promote methanol desorption, water does not change the methanol steady state reaction rate, while it has a substantial inhibiting effect on CH(4) formation. These results indicate that water can be used to increase the reaction selectivity to methanol and encourages further detailed investigations of the catalyst system.