A review of catalytic hydrodeoxygenation of lignin-derived phenols from biomass pyrolysis

被引:456
作者
Bu, Quan [1 ]
Lei, Hanwu [1 ]
Zacher, Alan H. [2 ]
Wang, Lu [1 ]
Ren, Shoujie [1 ]
Liang, Jing [1 ]
Wei, Yi [1 ]
Liu, Yupeng [1 ]
Tang, Juming [1 ]
Zhang, Qin [1 ]
Ruan, Roger [3 ]
机构
[1] Washington State Univ, Dept Biol Syst Engn, Bioprod Sci & Engn Lab, Richland, WA 99354 USA
[2] Pacific NW Natl Lab, Richland, WA 99354 USA
[3] Univ Minnesota, Dept Bioprod & Biosyst Engn, St Paul, MN 55108 USA
关键词
Lignin-derived phenols; Catalytic hydrodeoxygenation (HDO); Pyrolysis; Mechanism; Kinetics; BIO-OIL; TRANSPORTATION FUELS; MODEL COMPOUNDS; HYDROGEN; DEACTIVATION; CONVERSION; KINETICS; RESIDUE; HDO;
D O I
10.1016/j.biortech.2012.08.089
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Catalytic hydrodeoxygenation (HDO) of lignin-derived phenols which are the lowest reactive chemical compounds in biomass pyrolysis oils has been reviewed. The hydrodeoxygenation (HDO) catalysts have been discussed including traditional HDO catalysts such as CoMo/Al2O3 and NiMo/Al2O3 catalysts and transition metal catalysts (noble metals). The mechanism of HDO of lignin-derived phenols was analyzed on the basis of different model compounds. The kinetics of HDO of different lignin-derived model compounds has been investigated. The diversity of bio-oils leads to the complexities of HDO kinetics. The techno-economic analysis indicates that a series of major technical and economical efforts still have to be investigated in details before scaling up the HDO of lignin-derived phenols in existed refinery infrastructure. Examples of future investigation of HDO include significant challenges of improving catalysts and optimum operation conditions, further understanding of kinetics of complex bio-oils, and the availability of sustainable and cost-effective hydrogen source. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:470 / 477
页数:8
相关论文
共 74 条
[11]   Effects of support surface chemistry in hydrodeoxygenation reactions over CoMo/activated carbon sulfided catalysts [J].
de la Puente, G ;
Gil, A ;
Pis, JJ ;
Grange, P .
LANGMUIR, 1999, 15 (18) :5800-5806
[12]   Lignin Valorisation for Chemicals and (Transportation) Fuels via (Catalytic) Pyrolysis and Hydrodeoxygenation [J].
de Wild, Paul ;
Van der Laan, Ron ;
Kloekhorst, Arjan ;
Heeres, Erik .
ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2009, 28 (03) :461-469
[13]  
Diebold J.P., 2000, National Renewable Energy Laboratory Subcontractor Report
[14]   Synergy effect in the HDO of phenol over Ni-W catalysts supported on active carbon: Effect of tungsten precursors [J].
Echeandia, S. ;
Arias, P. L. ;
Barrio, V. L. ;
Pawelec, B. ;
Fierro, J. L. G. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2010, 101 (1-2) :1-12
[15]  
Elliot D.C., 2004, CHEM BIOMASS
[16]  
Elliott D., 1996, Developments in thermochemical biomass conversion, V1, P611
[17]   Historical developments in hydroprocessing bio-oils [J].
Elliott, Douglas C. .
ENERGY & FUELS, 2007, 21 (03) :1792-1815
[18]  
Freudenberg K., 1969, Science (80-.), V165, P784
[19]   Deactivation of hydroprocessing catalysts [J].
Furimsky, E ;
Massoth, FE .
CATALYSIS TODAY, 1999, 52 (04) :381-495
[20]   Catalytic hydrodeoxygenation [J].
Furimsky, E .
APPLIED CATALYSIS A-GENERAL, 2000, 199 (02) :147-190