Unraveling the mechanisms of ketene generation and transformation in syngas-to-olefin conversion over ZnCrO <sub> <i>x</i> </sub> |SAPO-34 catalysts

Ketene was identified as an intermediate in syngas-to-olefin (STO) conversion catalyzed by metal oxide-zeolite composites, which sparked a hot debate regarding its formation mechanism and catalytic roles. Here, we employed large-scale atomic simulations using global neural network potentials to explore the STO reaction pathways and microkinetic simulations to couple the reaction kinetics in ZnCrO <sub><i>x</i></sub> |SAPO-34 composite sites. Our results demonstrate that the majority of ketene (86.1%) originates from the methanol carbonylation-to-ketene route <i>via</i> nearby zeolite acidic sites, where methanol is produced through conventional syngas-to-methanol conversion on the Zn<sub>3</sub>Cr<sub>3</sub>O<sub>8</sub> (0001) surface, while the minority of ketene (13.9%) arises from a direct CHO*-CO* coupling pathway (CHO* + CO* + H* → CHOCO* + H* → CH<sub>2</sub>CO + O*) on Zn<sub>3</sub>Cr<sub>3</sub>O<sub>8</sub>. The presence of the ketene pathway significantly alters the catalytic performance in the zeolite, as methanol carbonylation to ketene is kinetically more efficient in competing with conventional methanol-to-olefins (MTO) conversion and thus predominantly drives the product to ethene. Based on our microkinetic simulation, it is the methanol carbonylation activity in the zeolite that dictates the performance of STO catalysts.

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Publication Details

Journal
Chemical Science
Published
2025-01-01
DOI
https://doi.org/10.1039/d5sc01651g
Citations
5
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
1.94

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article

Unraveling the mechanisms of ketene generation and transformation in syngas-to-olefin conversion over ZnCrO x |SAPO-34 catalysts

Zhi‐Pan Liu, Sicong Ma, Zhuo-Yan Yao
5 citations
Chemical Science
Catalysts for Methane Reforming
1.94
article

Unraveling the mechanisms of ketene generation and transformation in syngas-to-olefin conversion over ZnCrO x |SAPO-34 catalysts

Zhi‐Pan Liu, Sicong Ma, Zhuo-Yan Yao
article en
5 citations

Abstract

Ketene was identified as an intermediate in syngas-to-olefin (STO) conversion catalyzed by metal oxide-zeolite composites, which sparked a hot debate regarding its formation mechanism and catalytic roles. Here, we employed large-scale atomic simulations using global neural network potentials to explore the STO reaction pathways and microkinetic simulations to couple the reaction kinetics in ZnCrO <sub><i>x</i></sub> |SAPO-34 composite sites. Our results demonstrate that the majority of ketene (86.1%) originates from the methanol carbonylation-to-ketene route <i>via</i> nearby zeolite acidic sites, where methanol is produced through conventional syngas-to-methanol conversion on the Zn<sub>3</sub>Cr<sub>3</sub>O<sub>8</sub> (0001) surface, while the minority of ketene (13.9%) arises from a direct CHO*-CO* coupling pathway (CHO* + CO* + H* → CHOCO* + H* → CH<sub>2</sub>CO + O*) on Zn<sub>3</sub>Cr<sub>3</sub>O<sub>8</sub>. The presence of the ketene pathway significantly alters the catalytic performance in the zeolite, as methanol carbonylation to ketene is kinetically more efficient in competing with conventional methanol-to-olefins (MTO) conversion and thus predominantly drives the product to ethene. Based on our microkinetic simulation, it is the methanol carbonylation activity in the zeolite that dictates the performance of STO catalysts.

Chemical ScienceVol. 16(20)
Chinese Academy of Sciences (CN), Fudan University (CN), Shanghai Institute of Organic Chemistry (CN), Collaborative Innovation Center of Chemistry for Energy Materials (CN)
National Natural Science Foundation of China, Chinese Academy of Sciences, Science and Technology Commission of Shanghai Municipality, Youth Innovation Promotion Association of the Chinese Academy of Sciences, National Key Research and Development Program of China, Fundamental Research Funds for the Central Universities
Openalex Percentile: Top 15%
Catalysts for Methane Reforming
1.94
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