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DFT Analysis of Methane C−H Activation and Over-Oxidation by [Cu2O]2+ and [Cu2O2]2+ Sites in Zeolite Mordenite: Intra- versus Inter-site Over-Oxidation

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TLDR
In this paper, the role of dicopper [Cu3 O3 ]2+ sites in methane-to-methanol conversion was investigated using density functional theory (DFT) computations.
Abstract
Methane over-oxidation by copper-exchanged zeolites prevents realization of high-yield catalytic conversion. However, there has been little description of the mechanism for methane over-oxidation at the copper active sites of these zeolites. Using density functional theory (DFT) computations, we reported that tricopper [Cu3 O3 ]2+ active sites can over-oxidize methane. However, the role of [Cu3 O3 ]2+ sites in methane-to-methanol conversion remains under debate. Here, we examine methane over-oxidation by dicopper [Cu2 O]2+ and [Cu2 O2 ]2+ sites using DFT in zeolite mordenite (MOR). For [Cu2 O2 ]2+ , we considered the μ-(η2 :η2 ) peroxo-, and bis(μ-oxo) motifs. These sites were considered in the eight-membered (8MR) ring of MOR. μ-(η2 :η2 ) peroxo sites are unstable relative to the bis(μ-oxo) motif with a small interconversion barrier. Unlike [Cu2 O]2+ which is active for methane C-H activation, [Cu2 O2 ]2+ has a very large methane C-H activation barrier in the 8MR. Stabilization of methanol and methyl at unreacted dicopper sites however leads to over-oxidation via sequential hydrogen atom abstraction steps. For methanol, these are initiated by abstraction of the CH3 group, followed by OH and can proceed near 200 °C. Thus, for [Cu2 O]2+ and [Cu2 O2 ]2+ species, over-oxidation is an inter-site process. We discuss the implications of these findings for methanol selectivity, especially in comparison to the intra-site process for [Cu3 O3 ]2+ sites and the role of Bronsted acid sites.

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Journal ArticleDOI

Structure of Selective and Nonselective Dicopper (II) Sites in CuMFI for Methane Oxidation to Methanol

TL;DR: In this paper , the effect of the Si/Al ratio on the selectivity of the active dicopper sites in CuMFI has been investigated, and it has been shown that a higher Si-Al ratio leads to the formation of mono-μ-oxo dicoppers with Cu-Cu separation of 2.9 Å and a UV/vis absorption band at 27 200 cm-1 capable of selective oxidation of methane to methanol.
References
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Journal ArticleDOI

Metal dimer sites in ZSM-5 zeolite for methane-to-methanol conversion from first-principles kinetic modelling: is the [Cu–O–Cu]2+ motif relevant for Ni, Co, Fe, Ag, and Au?

TL;DR: In this article, the authors used first-principles microkinetic modeling to analyse the methane-to-methanol reaction on the [Cu-O-Cu]2+ motif, for Cu and other metals.
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On How Copper Mordenite Properties Govern the Framework Stability and Activity in the Methane-to-Methanol Conversion

TL;DR: In this paper, the authors investigated the activity of copper mordenites in the methane-to-methanol conversion and the material de-and realumination and found that the optimum stoichiometry between silicon, aluminum, and copper leads to a methanol productivity of up to 169 μmol/g.
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Formation of Active Cu-oxo Clusters for Methane Oxidation in Cu-Exchanged Mordenite

TL;DR: In this article, the selective oxidation of methane to methanol at moderate temperatures has been studied with the use of the Cu-exchanged mordenite (MOR) system.
Journal ArticleDOI

Pathways of Methane Transformation over Copper‐Exchanged Mordenite as Revealed by In Situ NMR and IR Spectroscopy

TL;DR: Observations are important for understanding the methane partial oxidation mechanism and for the rational design of the active materials for this reaction.
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Zeolite Surface Methoxy Groups as Key Intermediates in the Stepwise Conversion of Methane to Methanol

TL;DR: This article showed that surface methoxy groups (SMGs) located at zeolite Brønsted sites are the key intermediates in the Methane-to-Methanol (MTM) conversion over copper mordenite zeolites.
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