Hydrodeoxygenation of lignin phenolic derivatives to aromatics: A review of catalyst functionalization for targeted deoxygenation and active site modification strategies
J Yan, Z Li, Y Zhang, R Liu, L Zhou, P Fu - Fuel Processing Technology, 2023 - Elsevier
The catalytic hydrodeoxygenation of lignin phenolic derivatives to produce aromatic
hydrocarbons poses a significant challenge in achieving targeted cleavage of oxygen …
hydrocarbons poses a significant challenge in achieving targeted cleavage of oxygen …
Heterogeneously catalyzed ammoxidation: a valuable tool for one‐step synthesis of nitriles
A Martin, VN Kalevaru - ChemCatChem, 2010 - Wiley Online Library
Ammoxidation is a partial oxidation with selective insertion of nitrogen into a methyl group
(aldehyde or alcoholic groups are also able to react) that is in the α‐position to double …
(aldehyde or alcoholic groups are also able to react) that is in the α‐position to double …
Reactivity and stability investigation of supported molybdenum oxide catalysts for the hydrodeoxygenation (HDO) of m-cresol
The vapor-phase hydrodeoxygenation (HDO) of m-cresol is investigated at 593 K and H 2
pressures⩽ 1 bar for supported catalysts comprised of 10 wt% MoO 3 dispersed over SiO 2 …
pressures⩽ 1 bar for supported catalysts comprised of 10 wt% MoO 3 dispersed over SiO 2 …
Hydrodeoxygenation of guaiacol over carbon‐supported metal catalysts
J Chang, T Danuthai, S Dewiyanti, C Wang… - …, 2013 - Wiley Online Library
Catalytic bio‐oil upgrading to produce renewable fuels has attracted increasing attention in
response to the decreasing oil reserves and the increased fuel demand worldwide. Herein …
response to the decreasing oil reserves and the increased fuel demand worldwide. Herein …
Aqueous-phase hydrodeoxygenation of propanoic acid over the Ru/ZrO2 and Ru–Mo/ZrO2 catalysts
L Chen, Y Zhu, H Zheng, C Zhang, Y Li - Applied Catalysis A: General, 2012 - Elsevier
The conversion of propanoic acid under high hydrogen pressure has been studied over
zirconia-supported monometallic Ru and bimetallic Ru–Mo catalysts. The cleavage of C–C …
zirconia-supported monometallic Ru and bimetallic Ru–Mo catalysts. The cleavage of C–C …
Selective hydrodeoxygenation of 5-hydroxymethylfurfural to 2, 5-dimethylfuran on Ru–MoO x/C catalysts
Y Yang, Q Liu, D Li, J Tan, QI Zhang, C Wang, L Ma - RSC advances, 2017 - pubs.rsc.org
Selective hydrogenation of 5-hydroxymethylfurfural (HMF) has potential application in high
quality biofuels. Herein, the catalytic hydrodeoxygenation (HDO) of HMF to 2, 5 …
quality biofuels. Herein, the catalytic hydrodeoxygenation (HDO) of HMF to 2, 5 …
[HTML][HTML] Effect of composition and preparation of supported MoO3 catalysts for anisole hydrodeoxygenation
A series of zirconia supported molybdenum oxide materials with Mo loadings of 7, 12, and
19 wt% were synthesized using incipient wetness impregnation. The as synthesized oxide …
19 wt% were synthesized using incipient wetness impregnation. The as synthesized oxide …
Hydrodeoxygenation of lignin-derived phenolic compounds into aromatic hydrocarbons under low hydrogen pressure using molybdenum oxide as catalyst
MoO 3 catalyst was prepared by calcination using (NH 4) 6 Mo 7 O 24· 4H 2 O as precursor
and was characterized by XRD, XPS, H 2-TPR and low temperature N 2 adsorption …
and was characterized by XRD, XPS, H 2-TPR and low temperature N 2 adsorption …
Structural properties and reactivity trends of molybdenum oxide catalysts supported on zirconia for the hydrodeoxygenation of anisole
Vapor-phase hydrodeoxygenation (HDO) of anisole was investigated at 593 K and H2
pressures of≤ 1 bar over supported MoO3/ZrO2 catalysts with MoO3 loadings ranging from …
pressures of≤ 1 bar over supported MoO3/ZrO2 catalysts with MoO3 loadings ranging from …
[HTML][HTML] Effect of Co incorporation and support selection on deoxygenation selectivity and stability of (Co) Mo catalysts in anisole HDO
C Ranga, VI Alexiadis, J Lauwaert, R Lødeng… - Applied Catalysis A …, 2019 - Elsevier
A series of supported Co modified Mo catalysts was prepared by varying the Co/Mo ratio in
the range from 0 to 1 while maintaining the Mo loading at ca. 10 wt%. A sequential incipient …
the range from 0 to 1 while maintaining the Mo loading at ca. 10 wt%. A sequential incipient …