Synthesis of HZSM-5@activated carbon for improving aromatic production from catalytic pyrolysis of biomass
[Display omitted] •The novel catalyst HZSM-5@activated carbon was prepared and characterized.•Activated carbon supplied more acid sites and mesopores to the coated catalyst.•99.53% of aromatics with 75.68% of BTX were obtained from the catalytic pyrolysis.•Model compounds were used to help reveal th...
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Veröffentlicht in: | Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2024-08, Vol.494, p.153031, Article 153031 |
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Sprache: | eng |
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•The novel catalyst HZSM-5@activated carbon was prepared and characterized.•Activated carbon supplied more acid sites and mesopores to the coated catalyst.•99.53% of aromatics with 75.68% of BTX were obtained from the catalytic pyrolysis.•Model compounds were used to help reveal the biomass catalytic conversion pathway.•HZSM-5@activated carbon showed much lower coke yield (0.08%) than HZSM-5 (3.74%).
HZSM-5 widely used for the catalytic pyrolysis of biomass exhibits the drawbacks of high diffusion resistance and large coke production. To effectively enhance the catalytic efficiency and alleviate the coke deposition, a novel promising catalyst, HZSM-5 coated activated carbon (HZSM-5@AC), was prepared for the first time for in-line upgrading the pyrolysis products of soybean straw. Various catalysts including HZSM-5, activated carbon, and the HZSM-5@AC catalysts with different HZSM-5 to activated carbon mass ratios were characterized. The results showed that the HZSM-5 was successfully coated on the surface of activated carbon and the addition of activated carbon introduced a mesoporous structure and more acidic sites to the catalyst. The catalytic performance on the biomass conversion showed that the catalyst with HZSM-5-to-activated carbon mass ratio of 18:5 (18HZSM-5@5AC) had the highest catalytic efficiency on the conversion of biomass into aromatics with a selectivity of 99.5%, including 75.68% of benzene, toluene, and xylenes (BTX) with a yield of 74.68 mg/g. Moreover, a possible pathway for HZSM-5@AC catalyzed biomass pyrolysis was proposed through analyzing the conversion of model compounds. The catalyst cycling experiments demonstrated the higher stability of HZSM-5@AC than the parent HZSM-5 and activated carbon. TG, FTIR, Raman and SEM showed that the spent HZSM-5@AC was hardly structurally changed with a low coke yield of 0.08%. However, the spent HZSM-5 was partly structurally deactivated by large aromatic ring systems with a coke yield of 3.74%. SEM results also showed that a large amount of polymerized material encapsulated the surface of the spent HZSM-5. |
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ISSN: | 1385-8947 1873-3212 |
DOI: | 10.1016/j.cej.2024.153031 |