Catalysis Meets Nonthermal Separation for the Production of (Alkyl)phenols and Hydrocarbons from Pyrolysis Oil

被引:84
作者
Cao, Zhengwen [1 ]
Engelhardt, Jan [1 ]
Dierks, Michael [1 ]
Clough, Matthew T. [1 ]
Wang, Guang-Hui [1 ]
Heracleous, Eleni [2 ,3 ]
Lappas, Angelos [2 ,3 ]
Rinaldi, Roberto [4 ]
Schueth, Ferdi [1 ]
机构
[1] Max Planck Inst Kohlenforsch, D-45470 Mulheim, Germany
[2] Ctr Res & Technol Hellas, Chem Proc Engn Res Inst, POB 361, Thessaloniki 57001, Greece
[3] Int Hellen Univ, Sch Sci & Technol, POB 361, Thessaloniki 57001, Greece
[4] Imperial Coll London, Dept Chem Engn, South Kensington Campus, London SW7 2AZ, England
关键词
biomass; gas chromatography; hydrocarbons; molybdenum; phenols; SUPPORTED MOLYBDENUM CARBIDE; BIO-OIL; BIOMASS; HYDRODEOXYGENATION; CONVERSION; PHENOLS; LIGNIN; PHASE; FUELS; VALORIZATION;
D O I
10.1002/anie.201610405
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A simple and efficient hydrodeoxygenation strategy is described to selectively generate and separate high-value alkylphenols from pyrolysis bio-oil, produced directly from lignocellulosic biomass. The overall process is efficient and only requires low pressures of hydrogen gas (5 bar). Initially, an investigation using model compounds indicates that MoCx/C is a promising catalyst for targeted hydrodeoxygenation, enabling selective retention of the desired Ar-OH substituents. By applying this procedure to pyrolysis bio-oil, the primary products (phenol/4-alkylphenols and hydrocarbons) are easily separable from each other by short-path column chromatography, serving as potential valuable feedstocks for industry. The strategy requires no prior fractionation of the lignocellulosic biomass, no further synthetic steps, and no input of additional (e.g., petrochemical) platform molecules.
引用
收藏
页码:2334 / 2339
页数:6
相关论文
共 54 条
[21]   Catalytic hydrodeoxygenation [J].
Furimsky, E .
APPLIED CATALYSIS A-GENERAL, 2000, 199 (02) :147-190
[22]   Hydrotreatment of pyrolysis oils from biomass: Reactivity of the various categories of oxygenated compounds and preliminary techno-economical study [J].
Grange, P ;
Laurent, E ;
Maggi, R ;
Centeno, A ;
Delmon, B .
CATALYSIS TODAY, 1996, 29 (1-4) :297-301
[23]   Ni-Catalyzed Cleavage of Aryl Ethers in the Aqueous Phase [J].
He, Jiayue ;
Zhao, Chen ;
Lercher, Johannes A. .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2012, 134 (51) :20768-20775
[24]   Selective hydrogenolysis of phenols and phenyl ethers to arenes through direct C-O cleavage over ruthenium-tungsten bifunctional catalysts [J].
Huang, Yao-Bing ;
Yan, Long ;
Chen, Meng-Yuan ;
Guo, Qing-Xiang ;
Fu, Yao .
GREEN CHEMISTRY, 2015, 17 (05) :3010-3017
[25]   Production of liquid alkanes by aqueous-phase processing of biomass-derived carbohydrates [J].
Huber, GW ;
Chheda, JN ;
Barrett, CJ ;
Dumesic, JA .
SCIENCE, 2005, 308 (5727) :1446-1450
[26]   Production, separation and applications of phenolic-rich bio-oil - A review [J].
Kim, Joo-Sik .
BIORESOURCE TECHNOLOGY, 2015, 178 :90-98
[27]   Support and pretreatment effects on the hydrotreating activity of SBA-15 and CMK-5 supported nickel phosphide catalysts [J].
Koranyi, Tamas I. ;
Vit, Zdenek ;
Nagy, Janos B. .
CATALYSIS TODAY, 2008, 130 (01) :80-85
[28]  
Kropf C., 2015, US Patent, Patent No. [20,150,337,237, 20150337237]
[29]   Catalytic conversion of biomass to monofunctional hydrocarbons and targeted liquid-fuel classes [J].
Kunkes, Edward L. ;
Simonetti, Dante A. ;
West, Ryan M. ;
Serrano-Ruiz, Juan Carlos ;
Gartner, Christian A. ;
Dumesic, James A. .
SCIENCE, 2008, 322 (5900) :417-421
[30]   Precise oxygen scission of lignin derived aryl ethers to quantitatively produce aromatic hydrocarbons in water [J].
Luo, Zhicheng ;
Wang, Yimeng ;
He, Mingyuan ;
Zhao, Chen .
GREEN CHEMISTRY, 2016, 18 (02) :433-441