Hydrothermal conversion of xylose, glucose, and cellulose under the catalysis of transition metal sulfates

被引:75
作者
Cao, Xuefei [1 ]
Peng, Xinwen [1 ]
Sun, Shaoni [2 ]
Zhong, Linxin [1 ]
Chen, Wei [1 ]
Wang, Sha [1 ]
Sun, Run-Cang [1 ,2 ]
机构
[1] S China Univ Technol, State Key Lab Pulp & Paper Engn, Guangzhou 510640, Guangdong, Peoples R China
[2] Beijing Forestry Univ, Beijing Key Lab Lignocellulos Chem, Beijing 100083, Peoples R China
基金
中国国家自然科学基金;
关键词
Glucose; Cellulose; Hydrothermal conversion; Transition metal sulfates; Degradation correlation; HOT-COMPRESSED WATER; LEVULINIC ACID; SUPERCRITICAL WATER; SUBCRITICAL WATER; LACTIC-ACID; BIOMASS; DECOMPOSITION; LIQUEFACTION; FRUCTOSE; CHLORIDES;
D O I
10.1016/j.carbpol.2014.10.069
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Hydrothermal conversion (HTC) is an important thermochemical process to upgrade low-cost biomass into valuable chemicals or fuels. As compared with non-catalytic HTC, catalytic HTC shows high energy efficiency on biomass upgradation. In this work, the catalytic performances of various transition metal sulfates (Mn2+, Fe2+, Fe3+, Co2+, Ni2+, Cu2+, and Zn2+) in the HTCs of xylose, glucose, and cellulose under different conditions were explored. Among these catalysts, Zn2+ and Ni2+ showed obvious effects on the conversions of xylose, glucose, and cellulose into lactic acid, while Cu2+ and Fe3+, which could significantly accelerate the hydrolysis of cellulose into glucose at 200 degrees C, displayed high efficiency on converting glucose and cellulose into levulinic acid and formic acid at high temperature. Additionally, significant positive correlative relationships among xylose, glucose, and cellulose degradations were observed. This study is helpful for screening appropriate catalysts for biomass upgradation through catalytic HTC of monosaccharide. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:44 / 51
页数:8
相关论文
共 26 条
[1]   Reaction kinetics of D-xylose in sub- and supercritical water [J].
Aida, Taku Michael ;
Shiraishi, Naohiro ;
Kubo, Masaki ;
Watanabe, Masaru ;
Smith, Richard L., Jr. .
JOURNAL OF SUPERCRITICAL FLUIDS, 2010, 55 (01) :208-216
[2]   Domino Reaction Catalyzed by Zeolites with BrOnsted and Lewis Acid Sites for the Production of -Valerolactone from Furfural [J].
Bui, Linh ;
Luo, Helen ;
Gunther, William R. ;
Roman-Leshkov, Yuriy .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2013, 52 (31) :8022-8025
[3]   Conversion of xylose to levulinic acid over modified acid functions of alkaline-treated zeolite Y in hot-compressed water [J].
Chamnankid, Busaya ;
Ratanatawanate, Chalita ;
Faungnawakij, Kajornsak .
CHEMICAL ENGINEERING JOURNAL, 2014, 258 :341-347
[4]   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
[5]   Xylose Isomerization to Xylulose and its Dehydration to Furfural in Aqueous Media [J].
Choudhary, Vinit ;
Pinar, Ana B. ;
Sandler, Stanley I. ;
Vlachos, Dionisios G. ;
Lobo, Raul F. .
ACS CATALYSIS, 2011, 1 (12) :1724-1728
[6]   Catalytic conversion of cellulose to 5-hydroxymethyl furfural using acidic ionic liquids and co-catalyst [J].
Ding, Zhen-Dong ;
Shi, Jin-Cai ;
Xiao, Jing-Jing ;
Gu, Wen-Xiu ;
Zheng, Chang-Ge ;
Wang, Hai-Jun .
CARBOHYDRATE POLYMERS, 2012, 90 (02) :792-798
[7]   Chemical Conversion of Sugars to Lactic Acid by Alkaline Hydrothermal Processes [J].
Esposito, Davide ;
Antonietti, Markus .
CHEMSUSCHEM, 2013, 6 (06) :989-992
[8]   MECHANISM OF LEVULINIC ACID FORMATION [J].
HORVAT, J ;
KLAIC, B ;
METELKO, B ;
SUNJIC, V .
TETRAHEDRON LETTERS, 1985, 26 (17) :2111-2114
[9]   Kinetics of non-catalyzed decomposition of D-xylose in high temperature liquid water [J].
Jing Qi ;
Lue Xiuyang .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2007, 15 (05) :666-669
[10]   Glucose and fructose decomposition in subcritical and supercritical water: Detailed reaction pathway, mechanisms, and kinetics [J].
Kabyemela, BM ;
Adschiri, T ;
Malaluan, RM ;
Arai, K .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (08) :2888-2895