Fundamentals ofLi<sub>2</sub>CO<sub>3</sub>‑InducedEnhancement of C<sub>2</sub>H<sub>4</sub>/C<sub>2</sub>H<sub>6</sub> Selectivity in Oxidative Coupling of Methane over Mn-Na<sub>2</sub>WO<sub>4</sub>‑Based Catalysts

Oxidative coupling of methane (OCM) to C<sub>2</sub>H<sub>6</sub> and C<sub>2</sub>H<sub>4</sub> (C<sub>2</sub>-hydrocarbons) is an industrially attractive method for methane valorization. However, its commercialization is hampered by the low selectivity to C<sub>2</sub>-hydrocarbons, especially to C<sub>2</sub>H<sub>4</sub>. In this study, we demonstrate the use of a physical mixture of Li<sub>2</sub>CO<sub>3</sub> or LiNO<sub>3</sub> with differently supported catalysts based on the Mn-Na<sub>2</sub>WO<sub>4</sub> system for the efficient continuous formation of the target products using O<sub>2</sub> as an oxidant. The selectivity to C<sub>2</sub>-hydrocarbons and C<sub>2</sub>H<sub>4</sub> of 90.5 and 35.7% or 87.6 and 43.3%, respectively, was obtained at 7.2 or 13.3% CH<sub>4</sub> conversion over the Li<sub>2</sub>CO<sub>3</sub>-Mn-Na<sub>2</sub>WO<sub>4</sub>/Siral70 (AlSiO<sub><i>x</i></sub> with 70 wt % SiO<sub>2</sub>) catalyst, while its Li<sub>2</sub>CO<sub>3</sub>-free counterpart was unselective. Very similar performance is achieved by promoting the support with Li<sub>2</sub>CO<sub>3</sub> followed by deposition of the active components. In situ temperature-resolved and ex situ X-ray diffraction characterization studies showed that the promoter reacted completely with the active components and the support to yield highly crystalline materials with a low specific surface area. Such restructuring resulted in a strong improvement in the selectivity to C<sub>2</sub>-hydrocarbons due to inhibiting the direct heterogeneous oxidation of methane to carbon oxides. The selectivity changes were rationalized by steady-state isotopic transient kinetic analysis using OCM feeds with <sup>16</sup>O<sub>2</sub> or <sup>18</sup>O<sub>2</sub> and temporal analysis of products. Li<sub>2</sub>CO<sub>3</sub>-induced phase modifications affect both the concentration and lifetime of surface intermediates leading to CO<sub>2</sub> and CO. The knowledge gained provides guidance for the development of OCM catalysts with improved C<sub>2</sub>-selectivity. Moreover, the results obtained demonstrate the potential of our approach to elucidate the selectivity-governing factors relevant for tailored catalyst design and may stimulate future investigations of the development of selective catalysts in various alkane oxidation reactions.

Publication Details

Journal
Figshare
Published
2025-03-06
DOI
https://doi.org/10.1021/acscatal.5c00492.s001
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Catalysis and Oxidation Reactions
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article
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Fundamentals ofLi2CO3‑InducedEnhancement of C2H4/C2H6 Selectivity in Oxidative Coupling of Methane over Mn-Na2WO4‑Based Catalysts

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Catalysis and Oxidation Reactions
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Fundamentals ofLi2CO3‑InducedEnhancement of C2H4/C2H6 Selectivity in Oxidative Coupling of Methane over Mn-Na2WO4‑Based Catalysts

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Abstract

Oxidative coupling of methane (OCM) to C<sub>2</sub>H<sub>6</sub> and C<sub>2</sub>H<sub>4</sub> (C<sub>2</sub>-hydrocarbons) is an industrially attractive method for methane valorization. However, its commercialization is hampered by the low selectivity to C<sub>2</sub>-hydrocarbons, especially to C<sub>2</sub>H<sub>4</sub>. In this study, we demonstrate the use of a physical mixture of Li<sub>2</sub>CO<sub>3</sub> or LiNO<sub>3</sub> with differently supported catalysts based on the Mn-Na<sub>2</sub>WO<sub>4</sub> system for the efficient continuous formation of the target products using O<sub>2</sub> as an oxidant. The selectivity to C<sub>2</sub>-hydrocarbons and C<sub>2</sub>H<sub>4</sub> of 90.5 and 35.7% or 87.6 and 43.3%, respectively, was obtained at 7.2 or 13.3% CH<sub>4</sub> conversion over the Li<sub>2</sub>CO<sub>3</sub>-Mn-Na<sub>2</sub>WO<sub>4</sub>/Siral70 (AlSiO<sub><i>x</i></sub> with 70 wt % SiO<sub>2</sub>) catalyst, while its Li<sub>2</sub>CO<sub>3</sub>-free counterpart was unselective. Very similar performance is achieved by promoting the support with Li<sub>2</sub>CO<sub>3</sub> followed by deposition of the active components. In situ temperature-resolved and ex situ X-ray diffraction characterization studies showed that the promoter reacted completely with the active components and the support to yield highly crystalline materials with a low specific surface area. Such restructuring resulted in a strong improvement in the selectivity to C<sub>2</sub>-hydrocarbons due to inhibiting the direct heterogeneous oxidation of methane to carbon oxides. The selectivity changes were rationalized by steady-state isotopic transient kinetic analysis using OCM feeds with <sup>16</sup>O<sub>2</sub> or <sup>18</sup>O<sub>2</sub> and temporal analysis of products. Li<sub>2</sub>CO<sub>3</sub>-induced phase modifications affect both the concentration and lifetime of surface intermediates leading to CO<sub>2</sub> and CO. The knowledge gained provides guidance for the development of OCM catalysts with improved C<sub>2</sub>-selectivity. Moreover, the results obtained demonstrate the potential of our approach to elucidate the selectivity-governing factors relevant for tailored catalyst design and may stimulate future investigations of the development of selective catalysts in various alkane oxidation reactions.

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Catalysis and Oxidation Reactions
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Fundamentals ofLi<sub>2</sub>CO<sub>3</sub>‑InducedEnhancement of C<sub>2</sub>H<sub>4</sub>/C<sub>2</sub>H<sub>6</sub> Selectivity in Oxidative Coupling of Methane over Mn-Na<sub>2</sub>WO<sub>4</sub>‑Based Catalysts · Figshare (2025) | TGRS Research Map | TGRS