Synergistic catalysis strategy of Lewis and Brønsted acids for superior aromatic production in biomass pyrolysis

Catalytic pyrolysis is a versatile technology platform for converting biomass waste into valuable aromatics. However, achieving high yields and selectivity remains a significant challenge, particularly at low catalyst-to-biomass ratios. Herein, it is demonstrated that a novel bifunctional WO x /HZSM-5 zeolite catalyst featuring synergistic Brønsted/Lewis (B/L) acid sites is capable of significantly boosting aromatic production. Structural characterization shows that the incorporation of tungsten species leads to the formation of W–O–Si/Al structures, which generate new Lewis acid sites and optimize the B/L acid ratio. This precise tuning results in an impressive carbon yield of aromatic of 18.66 wt% with a catalyst-to-demineralized pine ratio as low as 2:1, demonstrating exceptional catalytic efficiency. Furthermore, our analysis reveals a nonlinear quadratic relationship between the B/L ratio and carbon yield of aromatic, highlighting the complex interplay between catalyst structure and performance. These findings provide a strategic avenue for acid site engineering in zeolite catalysts, advancing the efficient conversion of biomass into high-value aromatics. • High aromatic yield (18.66 wt%) is achieved with low catalyst-to-biomass ratio. • Tungsten species form W–O–Si/Al structures, generating new Lewis acid sites. • Nonlinear relationship discovered between B/L ratio and aromatic yield.

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Publication Details

Journal
Industrial Crops and Products
Published
2025-02-18
DOI
https://doi.org/10.1016/j.indcrop.2025.120710
Citations
4
Primary Topic
Zeolite Catalysis and Synthesis
Type
article
Field-Weighted Citation Impact
2.15

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article

Synergistic catalysis strategy of Lewis and Brønsted acids for superior aromatic production in biomass pyrolysis

Shengpeng Xia, Jionghua Ou, Anqing Zheng, Zengli Zhao et al.
4 citations
Industrial Crops and Products
Zeolite Catalysis and Synthesis
2.15
article

Synergistic catalysis strategy of Lewis and Brønsted acids for superior aromatic production in biomass pyrolysis

Shengpeng Xia, Jionghua Ou, Anqing Zheng, Zengli Zhao, Kun Zhao, Shu Chen, Zhihao Wang, Jiaqi Liang
article en
4 citations

Abstract

Catalytic pyrolysis is a versatile technology platform for converting biomass waste into valuable aromatics. However, achieving high yields and selectivity remains a significant challenge, particularly at low catalyst-to-biomass ratios. Herein, it is demonstrated that a novel bifunctional WO x /HZSM-5 zeolite catalyst featuring synergistic Brønsted/Lewis (B/L) acid sites is capable of significantly boosting aromatic production. Structural characterization shows that the incorporation of tungsten species leads to the formation of W–O–Si/Al structures, which generate new Lewis acid sites and optimize the B/L acid ratio. This precise tuning results in an impressive carbon yield of aromatic of 18.66 wt% with a catalyst-to-demineralized pine ratio as low as 2:1, demonstrating exceptional catalytic efficiency. Furthermore, our analysis reveals a nonlinear quadratic relationship between the B/L ratio and carbon yield of aromatic, highlighting the complex interplay between catalyst structure and performance. These findings provide a strategic avenue for acid site engineering in zeolite catalysts, advancing the efficient conversion of biomass into high-value aromatics. • High aromatic yield (18.66 wt%) is achieved with low catalyst-to-biomass ratio. • Tungsten species form W–O–Si/Al structures, generating new Lewis acid sites. • Nonlinear relationship discovered between B/L ratio and aromatic yield.

Industrial Crops and ProductsVol. 226
University of Science and Technology of China (CN), Guangzhou Institute of Energy Conversion (CN), University of Chinese Academy of Sciences (CN), Guangdong Ocean University (CN), Zhongkai University of Agriculture and Engineering (CN)
National Natural Science Foundation of China, Natural Science Foundation of Guangdong Province
Openalex Percentile: Top 14%
Zeolite Catalysis and Synthesis
2.15
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