Aqueous-phase hydrogenolysis of glucose to value-added chemicals and biofuels: A comparative study of active metals

被引:37
作者
Liu, Chengwei [1 ,3 ]
Zhang, Chenghua [1 ,2 ]
Liu, Kangkai [2 ]
Wang, Yi [2 ]
Fan, Gaixian [2 ]
Sun, Sikai [2 ]
Xu, Jian [2 ]
Zhu, Yulei [1 ,2 ]
Li, Yongwang [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Coal Chem, State Key Lab Coal Convers, Taiyuan 030001, Peoples R China
[2] Synfuels CHINA Co Ltd, Natl Energy Ctr Coal Liquids, Beijing 101400, Peoples R China
[3] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
关键词
Glucose; Hydrogenolysis; Chemicals; Biofuels; Transition metals; CATALYTIC CONVERSION; REACTION PATHWAYS; ETHYLENE-GLYCOL; HYDROGENATION; SORBITOL; RUTHENIUM; CELLULOSE; FRUCTOSE; BIOMASS; SUGAR;
D O I
10.1016/j.biombioe.2014.11.005
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Glucose is the most abundant platform molecule of biomass in nature. High value-added chemicals and liquid fuels can be obtained by selectively breaking C-C/C-O bonds and removing surplus oxygen in glucose. This article focuses on glucose hydrogenolysis over a wide variety of transition metal catalysts (Cu/C, Ni/C, Pt/C, Pd/C, Ru/C, Rh/C, Ir/C). Liquid and gas phase after reaction mainly contain three types of products such as polyols, alkanes, furans. Many value-added chemicals and liquid fuels were obtained, such as sorbitol, 1,2-propanediol, ethylene glycol, 2,5-dimethylfuran, 2,5-dimethyltetrahydrofuran, hexane, etc. Different metal catalysts showed different selectivities to these products. Typically, at hydrogenation conditions of 453 K and 4.0 MPa, glucose was largely converted to C-1 products over the Ru/C catalyst. Pd/C selectively converted glucose into C-2 and C-3 products. C-6 products were most selective over Pt/C. The hydrogenation/hydrogenolysis capabilities of different metals for C-C and C-O bonds, the endocyclic C=C and C-O-C bonds are also quite different. For example, Pt/C provides the weakest hydrogenolysis activity to C-O and C-C bonds. Ru/C possesses the highest activity to C-C and C-O bond cleavage. Meanwhile, it is most active for C-O-C bond hydrogenation in glucose at low temperature. Cu/C exhibits the weakest endocyclic C=C bond hydrogenation activity in furan ring. The reaction pathway of glucose hydrogenolysis over different metal catalysts was also outlined. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:189 / 199
页数:11
相关论文
共 51 条
[1]  
AKHER MA, 1974, STARKE, V26, P307
[2]  
Arena B. J., 1985, US. Pat, Patent No. [4 496 780, 4496780, 4,496,780]
[3]   Hydrogenolysis of sorbitol over Ni and Pt loaded on NaY [J].
Banu, M. ;
Sivasanker, S. ;
Sankaranarayanan, T. M. ;
Venuvanalingam, P. .
CATALYSIS COMMUNICATIONS, 2011, 12 (07) :673-677
[4]   Simple Chemical Transformation of Lignocellulosic Biomass into Furans for Fuels and Chemicals [J].
Binder, Joseph B. ;
Raines, Ronald T. .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2009, 131 (05) :1979-1985
[5]   Starch-derived polyols for polymer technologies: preparation by hydrogenolysis on metal catalysts [J].
Blanc, B ;
Bourrel, A ;
Gallezot, P ;
Haas, T ;
Taylor, P .
GREEN CHEMISTRY, 2000, 2 (02) :89-91
[6]   One-Pot Conversion of Sugar and Sugar Polyols to n-Alkanes without C-C Dissociation over the Ir-ReOx/SiO2 Catalyst Combined with H-ZSM-5 [J].
Chen, Kaiyou ;
Tamura, Masazumi ;
Yuan, Zhenle ;
Nakagawa, Yoshinao ;
Tomishige, Keiichi .
CHEMSUSCHEM, 2013, 6 (04) :613-621
[7]   Hydrogenolysis of biomass-derived sorbitol to glycols and glycerol over Ni-MgO catalysts [J].
Chen, Xinguo ;
Wang, Xicheng ;
Yao, Shengxi ;
Mu, Xindong .
CATALYSIS COMMUNICATIONS, 2013, 39 :86-89
[8]   Liquid-phase catalytic processing of biomass-derived oxygenated hydrocarbons to fuels and chemicals [J].
Chheda, Juben N. ;
Huber, George W. ;
Dumesic, James A. .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2007, 46 (38) :7164-7183
[9]  
Chopade S. P., 2001, US Patent, Patent No. [US6291725B1, 6291725]
[10]   HYDROGENOLYSIS OF SORBITOL [J].
CLARK, IT .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (08) :1125-1126