Low temperature catalytic hydrodeoxygenation of lignin-derived phenols to cyclohexanols over the Ru/SBA-15 catalyst
Cyclohexanol and its derivatives are widely used as chemical intermediates and fuel additives. Herein, Ru/SBA-15 catalysts were prepared via impregnation, and used for the production of cyclohexanols from lignin-derived phenols. The catalyst samples were characterized by XRD, XPS, TEM, etc., where t...
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Format: | Article |
Language: | English |
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Royal Society of Chemistry
2022
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Online Access: | View Fulltext in Publisher |
LEADER | 02393nam a2200469Ia 4500 | ||
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001 | 10.1039-d2ra01183b | ||
008 | 220425s2022 CNT 000 0 und d | ||
020 | |a 20462069 (ISSN) | ||
245 | 1 | 0 | |a Low temperature catalytic hydrodeoxygenation of lignin-derived phenols to cyclohexanols over the Ru/SBA-15 catalyst |
260 | 0 | |b Royal Society of Chemistry |c 2022 | |
300 | |a 11 | ||
856 | |z View Fulltext in Publisher |u https://doi.org/10.1039/d2ra01183b | ||
520 | 3 | |a Cyclohexanol and its derivatives are widely used as chemical intermediates and fuel additives. Herein, Ru/SBA-15 catalysts were prepared via impregnation, and used for the production of cyclohexanols from lignin-derived phenols. The catalyst samples were characterized by XRD, XPS, TEM, etc., where the Ru0 species was speculated as the active phase. 5 wt% Ru/SBA-15 with small Ru particle size (4.99 nm) and high Ru dispersion (27.05%) exhibited an excellent hydrogenation activity. A high cyclohexanol yield of >99.9% was achieved at 20 °C for 5 h in an aqueous phase, and the catalyst indicated stable activity and selectivity after five runs. Crucially, Ru/SBA-15 exhibited a zero-order reaction rate with an apparent activation energy (Ea) as low as 10.88 kJ mol−1 and a TON of 172.84 at 80 °C. Simultaneously, demethoxylation activity was also observed in the hydrodeoxygenation (HDO) of G- and S-type monophenols, and a high yield of 37.4% of cyclohexanol was obtained at 80 °C and 4 h when using eugenol as substrate. © 2022 The Royal Society of Chemistry | |
650 | 0 | 4 | |a Activation energy |
650 | 0 | 4 | |a Activation Energy |
650 | 0 | 4 | |a Active phasis |
650 | 0 | 4 | |a Catalyst activity |
650 | 0 | 4 | |a Catalyst selectivity |
650 | 0 | 4 | |a Chemical intermediates |
650 | 0 | 4 | |a Cyclohexanol |
650 | 0 | 4 | |a Fuel additives |
650 | 0 | 4 | |a Hydrodeoxygenation |
650 | 0 | 4 | |a Lignin |
650 | 0 | 4 | |a Lignin-derived phenol |
650 | 0 | 4 | |a Lows-temperatures |
650 | 0 | 4 | |a Particle size |
650 | 0 | 4 | |a Particle Size |
650 | 0 | 4 | |a Particles sizes |
650 | 0 | 4 | |a Phenols |
650 | 0 | 4 | |a Phenols |
650 | 0 | 4 | |a Ruthenium |
650 | 0 | 4 | |a Ruthenium |
650 | 0 | 4 | |a SBA-15 catalysts |
650 | 0 | 4 | |a Temperature |
650 | 0 | 4 | |a Temperature |
650 | 0 | 4 | |a XRD |
700 | 1 | |a Feng, S. |e author | |
700 | 1 | |a Hu, C. |e author | |
700 | 1 | |a Li, G. |e author | |
700 | 1 | |a Liu, X. |e author | |
700 | 1 | |a Su, Z. |e author | |
773 | |t RSC Advances |