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Oxidation of methane to methanol on the surface of FeZSM-5 zeolite
Methane oxidation by N2O was studied at 160°C on the FeZSM-5 surface with increased concentration of α-sites (100μmol/g). The reaction was shown to lead directly to methanol. Spillover of methanol from α-sites provides a “quasicatalytic” mode of the reaction with TON>3. [Display omitted] ► Methan...
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Published in: | Journal of catalysis 2013-04, Vol.300, p.47-54 |
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Main Authors: | , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Methane oxidation by N2O was studied at 160°C on the FeZSM-5 surface with increased concentration of α-sites (100μmol/g). The reaction was shown to lead directly to methanol. Spillover of methanol from α-sites provides a “quasicatalytic” mode of the reaction with TON>3. [Display omitted]
► Methane oxidation by N2O on FeZSM-5 α-sites at 160°C leads directly to methanol. ► Methanol spillovers from α-sites providing “quasicatalytic” mode of reaction (TON>3). ► A part of methanol is converted to DME and non-extractable products.
In our previous work using FeZSM-5 zeolite with increased concentration of α-sites (100μmol/g), the oxidation of methane by α-oxygen predeposited from nitrous oxide was studied at room temperature. The reaction proceeded by hydrogen abstraction mechanism yielding methoxy and hydroxy groups bound to α-sites.
The present work conducted with the same zeolite is devoted to methane oxidation by N2O in the process of α-oxygen deposition at 160°С. Under these conditions, the reaction was shown to proceed at a stoichiometric ratio СН4:N2O=1:1 yielding directly methanol. Spillover of methanol from α-sites liberates them for further events of α-oxygen deposition, thus converting the reaction to a “quasicatalytic” mode that runs up to turnover number exceeding 3 with no product desorption into the gas phase. A part of methanol is converted to dimethyl ether, traces of acetaldehyde, and some amount of non-extractable products.
Mechanism of the reaction is discussed. |
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ISSN: | 0021-9517 1090-2694 |
DOI: | 10.1016/j.jcat.2012.12.030 |