Mechanistic insights into coke suppression and enhanced olefin selectivity in mixed metal oxide-modified SAPO-34 for high-performance methanol-to-olefins catalysis

• Higher olefin selectivity : SPM achieves 85.7 % total olefin selectivity, surpassing SP (76.6 %). • Extended catalyst lifespan : SPM maintains stability nearly twice as long as SP. • Optimized propylene yield : SPM enhances P/E ratio (2.9 vs. 1.5 in SP). • Improved porosity and acidity : Enhanced mass transfer reduces coke formation. • Effective coke suppression : MD simulations confirm reduced coke precursor formation and promoted coke oxidation. The methanol-to-olefins (MTO) process is a key catalytic route for light olefin production, yet challenges related to catalyst deactivation and coke formation persist. In this study, we investigate the catalytic performance of SAPO-34 (SP) and a modified SAPO-34 catalyst incorporating a mixed metal oxide of indium oxide and cerium oxide (SPM) to enhance selectivity, stability, and coke resistance. A combination of experimental and theoretical approaches, including catalyst characterization, MTO catalytic testing, and molecular dynamics (MD) simulations, was employed to elucidate the impact of mixed metal oxide incorporation on catalyst properties. The results indicate that SPM exhibits significantly higher total olefin selectivity (85.7 %) compared to SP (76.6 %), with improved stability and a catalytic lifetime approximately twice as long. Furthermore, SPM demonstrates a higher propylene-to-ethylene (P/E) ratio, reaching 2.9 at the initial stage compared to 1.5 for SP. The incorporation of mixed metal oxides enhances mesoporosity and modifies acid site distribution, reducing excessive secondary reactions and mitigating coke formation. MD simulations confirm that SPM inhibits the formation of formaldehyde species, a key coke precursor, while promoting coke oxidation, thereby extending catalyst lifespan. These findings suggest that mixed metal oxide incorporation is an effective strategy for optimizing SAPO-34-based catalysts for sustainable MTO applications.

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Publication Details

Journal
Chemical Engineering Journal Advances
Published
2025-04-08
DOI
https://doi.org/10.1016/j.ceja.2025.100745
Citations
15
Primary Topic
Zeolite Catalysis and Synthesis
Type
article
Field-Weighted Citation Impact
8.06

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article

Mechanistic insights into coke suppression and enhanced olefin selectivity in mixed metal oxide-modified SAPO-34 for high-performance methanol-to-olefins catalysis

Jafar Towfighi, Masoud Safari Yazd, Alireza Abbasi, Mohammad Reza Pourmand
15 citations
Chemical Engineering Journal Advances
Zeolite Catalysis and Synthesis
8.06
article

Mechanistic insights into coke suppression and enhanced olefin selectivity in mixed metal oxide-modified SAPO-34 for high-performance methanol-to-olefins catalysis

Jafar Towfighi, Masoud Safari Yazd, Alireza Abbasi, Mohammad Reza Pourmand
article en
15 citations

Abstract

• Higher olefin selectivity : SPM achieves 85.7 % total olefin selectivity, surpassing SP (76.6 %). • Extended catalyst lifespan : SPM maintains stability nearly twice as long as SP. • Optimized propylene yield : SPM enhances P/E ratio (2.9 vs. 1.5 in SP). • Improved porosity and acidity : Enhanced mass transfer reduces coke formation. • Effective coke suppression : MD simulations confirm reduced coke precursor formation and promoted coke oxidation. The methanol-to-olefins (MTO) process is a key catalytic route for light olefin production, yet challenges related to catalyst deactivation and coke formation persist. In this study, we investigate the catalytic performance of SAPO-34 (SP) and a modified SAPO-34 catalyst incorporating a mixed metal oxide of indium oxide and cerium oxide (SPM) to enhance selectivity, stability, and coke resistance. A combination of experimental and theoretical approaches, including catalyst characterization, MTO catalytic testing, and molecular dynamics (MD) simulations, was employed to elucidate the impact of mixed metal oxide incorporation on catalyst properties. The results indicate that SPM exhibits significantly higher total olefin selectivity (85.7 %) compared to SP (76.6 %), with improved stability and a catalytic lifetime approximately twice as long. Furthermore, SPM demonstrates a higher propylene-to-ethylene (P/E) ratio, reaching 2.9 at the initial stage compared to 1.5 for SP. The incorporation of mixed metal oxides enhances mesoporosity and modifies acid site distribution, reducing excessive secondary reactions and mitigating coke formation. MD simulations confirm that SPM inhibits the formation of formaldehyde species, a key coke precursor, while promoting coke oxidation, thereby extending catalyst lifespan. These findings suggest that mixed metal oxide incorporation is an effective strategy for optimizing SAPO-34-based catalysts for sustainable MTO applications.

Chemical Engineering Journal AdvancesVol. 22
Tarbiat Modares University (IR)
Iran National Science Foundation
Openalex Percentile: Top 2%
Zeolite Catalysis and Synthesis
8.06
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