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...

Full description

Bibliographic Details
Main Authors: Feng, S. (Author), Hu, C. (Author), Li, G. (Author), Liu, X. (Author), Su, Z. (Author)
Format: Article
Language:English
Published: Royal Society of Chemistry 2022
Subjects:
XRD
Online Access:View Fulltext in Publisher
LEADER 02393nam a2200469Ia 4500
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