Hierarchical Mo/HTNU-9 boosts methane aromatization with mitigated carbon deposition

Methane dehydroaromatization (MDA) offers a promising route for converting methane into aromatics, yet rapid catalyst deactivation via coking remains a critical barrier. This study addresses this challenge through TPAOH-assisted hierarchical pore engineering of HTNU-9 zeolite. Controlled desilication (0.25 mol/L TPAOH, 24 h) generates micro-mesoporous Mo/HTNU-9-24 while retaining microporous integrity, achieving a 22 % increase in methane conversion (14.7 % vs. 11.4 % for pristine Mo/HTNU-9) at 700 °C. The hierarchical architecture enhances mass transfer and Mo dispersion via synergistic effects. Silanol-rich mesopore surfaces and mild alkalinity stabilize Mo species, selective removal of strong acid sites coupled with spatial confinement of mesopores mitigate coke accumulation. The optimized catalyst exhibits prolonged stability due to restricted Mo agglomeration and efficient carbon precursor diffusion. These findings establish a dual strategy (pore topology control and acid site modulation) to synchronize active center dynamics and coke resistance, advancing the rational design of hierarchical zeolites for industrial MDA applications. Hierarchical Mo/HTNU-9-24, engineered via TPAOH-assisted desilication, integrates micro-mesoporous networks for optimized Mo dispersion and accelerated product diffusion. Mo/HTNU-9-24 achieves a 22 % boost in CH 4 conversion (14.7 %) and prolonged stability. • TPAOH-assisted hierarchical TNU-9 has been successfully prepared. • Methane conversion reached 14.7 % over Mo/HTNU-9-24. • Mo/HTNU-9-24 shows better catalytic stability than pristine Mo/TNU-9.

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Publication Details

Journal
Fuel Processing Technology
Published
2025-09-02
DOI
https://doi.org/10.1016/j.fuproc.2025.108323
Citations
1
Primary Topic
Catalytic Processes in Materials Science
Type
article
Field-Weighted Citation Impact
0.52
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article

Hierarchical Mo/HTNU-9 boosts methane aromatization with mitigated carbon deposition

Chunxue Yang, Jing Hu, Jingjing Tian, Xin Kang et al.
1 citations
Fuel Processing Technology
Catalytic Processes in Materials Science
0.52
article

Hierarchical Mo/HTNU-9 boosts methane aromatization with mitigated carbon deposition

Chunxue Yang, Jing Hu, Jingjing Tian, Xin Kang, Xiaohui Wang, Xiaodong Chen, Jinglin Liu
article en
1 citations

Abstract

Methane dehydroaromatization (MDA) offers a promising route for converting methane into aromatics, yet rapid catalyst deactivation via coking remains a critical barrier. This study addresses this challenge through TPAOH-assisted hierarchical pore engineering of HTNU-9 zeolite. Controlled desilication (0.25 mol/L TPAOH, 24 h) generates micro-mesoporous Mo/HTNU-9-24 while retaining microporous integrity, achieving a 22 % increase in methane conversion (14.7 % vs. 11.4 % for pristine Mo/HTNU-9) at 700 °C. The hierarchical architecture enhances mass transfer and Mo dispersion via synergistic effects. Silanol-rich mesopore surfaces and mild alkalinity stabilize Mo species, selective removal of strong acid sites coupled with spatial confinement of mesopores mitigate coke accumulation. The optimized catalyst exhibits prolonged stability due to restricted Mo agglomeration and efficient carbon precursor diffusion. These findings establish a dual strategy (pore topology control and acid site modulation) to synchronize active center dynamics and coke resistance, advancing the rational design of hierarchical zeolites for industrial MDA applications. Hierarchical Mo/HTNU-9-24, engineered via TPAOH-assisted desilication, integrates micro-mesoporous networks for optimized Mo dispersion and accelerated product diffusion. Mo/HTNU-9-24 achieves a 22 % boost in CH 4 conversion (14.7 %) and prolonged stability. • TPAOH-assisted hierarchical TNU-9 has been successfully prepared. • Methane conversion reached 14.7 % over Mo/HTNU-9-24. • Mo/HTNU-9-24 shows better catalytic stability than pristine Mo/TNU-9.

Fuel Processing TechnologyVol. 277
Inner Mongolia University for Nationalities (CN)
Openalex Percentile: Top 34%
Catalytic Processes in Materials Science
0.52
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