Catalytic hydrodeoxygenation (HDO) of phenol over supported molybdenum carbide, nitride, phosphide and oxide catalysts

被引:208
作者
Boullosa-Eiras, Sara [1 ]
Lodeng, Rune [2 ]
Bergem, Hakon [2 ]
Stocker, Michael [3 ]
Hannevold, Lenka [3 ]
Blekkana, Edd A. [1 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Chem Engn, N-7491 Trondheim, Norway
[2] SINTEF Mat & Chem, Dept Kinet & Catalysis, N-7465 Trondheim, Norway
[3] SINTEF Mat & Chem, Dept Proc Intensificat & Catalysis, N-0314 Oslo, Norway
关键词
Bio-oil; Hydrodeoxygenation; Phenol; Phosphides; Carbides; Nitrides; TRANSITION-METAL PHOSPHIDES; METHYL-SUBSTITUTED PHENOLS; HYDROPROCESSING CATALYSTS; MODEL-COMPOUND; PYROLYSIS OIL; HYDRODESULFURIZATION; GUAIACOL; BIOMASS; HYDRODENITROGENATION; DIBENZOTHIOPHENE;
D O I
10.1016/j.cattod.2013.09.044
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The performance of titania-supported molybdenum carbide, nitride, phosphide and oxide catalysts was compared for catalytic hydrodeoxygenation (HDO) of phenol. Phenol was selected as a stable model component for lignin degradation products in fast pyrolysis bio-oil. The synthesis and formation path of the materials was evaluated by the use of complementary characterization techniques (XRD, TPR and TGA-MS). All the catalysts showed promising catalytic performance during testing in a fixed-bed reactor set-up at a temperature of 350 degrees C and total pressure of 25 bar, and the highest activity was achieved with 15 wt% Mo2C/TiO2. A high selectivity towards benzene was observed with all catalysts. MoP supported on TiO2 showed the strongest tendency to aromatic ring hydrogenation and also a significant selectivity (10% level) towards methylcyclopentane, indicating contributions of acidic surface chemistry. Thus, Mo based materials are active and promising materials for establishing selectivity control in HDO of bio-oils. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:44 / 53
页数:10
相关论文
共 52 条
[1]   ALKALI PROMOTION OF ALUMINA-SUPPORTED COBALT FISCHER-TROPSCH CATALYSTS STUDIED BY TPR, TPD AND PULSE CHEMISORPTION [J].
BLEKKAN, EA ;
HOLMEN, A ;
VADA, S .
ACTA CHEMICA SCANDINAVICA, 1993, 47 (03) :275-280
[2]   A review of catalytic hydrodeoxygenation of lignin-derived phenols from biomass pyrolysis [J].
Bu, Quan ;
Lei, Hanwu ;
Zacher, Alan H. ;
Wang, Lu ;
Ren, Shoujie ;
Liang, Jing ;
Wei, Yi ;
Liu, Yupeng ;
Tang, Juming ;
Zhang, Qin ;
Ruan, Roger .
BIORESOURCE TECHNOLOGY, 2012, 124 :470-477
[3]   A novel method for preparing an active nickel phosphide catalyst for HDS of dibenzothiophene [J].
Cecilia, J. A. ;
Infantes-Molina, A. ;
Rodriguez-Castellon, E. ;
Jimenez-Lopez, A. .
JOURNAL OF CATALYSIS, 2009, 263 (01) :4-15
[4]   Influence of the degree of carburization on the density of sites and hydrogenating activity of molybdenum carbides [J].
Choi, JS ;
Bugli, G ;
Djéga-Mariadassou, G .
JOURNAL OF CATALYSIS, 2000, 193 (02) :238-247
[5]   Alumina-supported molybdenum phosphide hydroprocessing catalysts [J].
Clark, PA ;
Oyama, ST .
JOURNAL OF CATALYSIS, 2003, 218 (01) :78-87
[6]   THE STRUCTURE AND FUNCTION OF SUPPORTED MOLYBDENUM NITRIDE HYDRODENITROGENATION CATALYSTS [J].
COLLING, CW ;
THOMPSON, LT .
JOURNAL OF CATALYSIS, 1994, 146 (01) :193-203
[7]   Hydrodeoxygenation of lignin model compounds over a copper chromite catalyst [J].
Deutsch, Keenan L. ;
Shanks, Brent H. .
APPLIED CATALYSIS A-GENERAL, 2012, 447 :144-150
[8]   Simultaneous hydrodesulfurization, hydrodeoxygenation, and hydrogenation with molybdenum carbide [J].
Dhandapani, B ;
St Clair, T ;
Oyama, ST .
APPLIED CATALYSIS A-GENERAL, 1998, 168 (02) :219-228
[9]   Hydrotreatment activities of supported molybdenum nitrides and carbides [J].
Dolce, GM ;
Savage, PE ;
Thompson, LT .
ENERGY & FUELS, 1997, 11 (03) :668-675
[10]   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