Fractionating recalcitrant lignocellulose at modest reaction conditions

被引:456
作者
Zhang, Yi-Heng Percival [1 ]
Ding, Shi-You
Mielenz, Jonathan R.
Cui, Jing-Biao
Elander, Richard T.
Laser, Mark
Himmel, Michael E.
McMillan, James R.
Lynd, Lee R.
机构
[1] Virginia Polytech Inst & State Univ, Dept Biol Syst Engn, Blacksburg, VA 24061 USA
[2] Natl Renewable Energy Lab, Natl Bioenergy Ctr, Golden, CO 80401 USA
[3] Oak Ridge Natl Lab, Div Life Sci, Oak Ridge, TN 37831 USA
[4] Dartmouth Coll, Thayer Sch Engn, Hanover, NH 03755 USA
[5] Dartmouth Coll, Ctr Nanomat Res, Hanover, NH 03755 USA
关键词
biorefinery; cellulose hydrolysis; cellulosic ethanol; lignocellulose fractionation;
D O I
10.1002/bit.21386
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Effectively releasing the locked polysaccharides from recalcitrant lignocellulose to fermentable sugars is among the greatest technical and economic barriers to the realization of lignocellulose biorefineries because leading lignocellulose pre-treatment technologies suffer from low sugar yields, and/or severe reaction conditions, and/or high cellulase use, narrow substrate applicability, and high capital investment, etc. A new lignocellulose pre-treatment featuring modest reaction conditions (50 degrees C and atmospheric pressure) was demonstrated to fractionate lignocellulose to amorphous cellulose, hemicellulose, lignin, and acetic acid by using a non-volatile cellulose solvent (concentrated phosphoric acid), a highly volatile organic solvent (acetone), and water. The highest sugar yields after enzymatic hydrolysis were attributed to no sugar degradation during the fractionation and the highest enzymatic cellulose digestibility (similar to 97% in 24 h) during the hydrolysis step at the enzyme loading of 15 filter paper units of cellulase and 60 IU of beta-glucosidase per gram of glucan. Isolation of high-value lignocellulose components (lignin, acetic acid, and hemicellulose) would greatly increase potential revenues of a lignocellulose biorefinery.
引用
收藏
页码:214 / 223
页数:10
相关论文
共 58 条
[1]   The lignol approach to biorefining of woody biomass to produce ethanol and chemicals [J].
Claudio Arato ;
E. Kendall Pye ;
Gordon Gjennestad .
Applied Biochemistry and Biotechnology, 2005, 123 (1-3) :871-882
[2]  
AZIZ S, 1989, TAPPI J, V72, P169
[3]  
Biomass Research and Development Technical Advisory Committee, 2002, ROADM BIOM TECHN US
[4]   Climate sensitivity uncertainty and the need for energy without CO2 emission [J].
Caldeira, K ;
Jain, AK ;
Hoffert, MI .
SCIENCE, 2003, 299 (5615) :2052-2054
[5]   Enhancement of cellulose saccharification kinetics using an ionic liquid pretreatment step [J].
Dadi, Anantharam P. ;
Varanasi, Sasidhar ;
Schall, Constance A. .
BIOTECHNOLOGY AND BIOENGINEERING, 2006, 95 (05) :904-910
[6]  
Davis ME, 2002, J ANIM SCI, V80, P2887
[7]   Cellulase, clostridia, and ethanol [J].
Demain, AL ;
Newcomb, M ;
Wu, JHD .
MICROBIOLOGY AND MOLECULAR BIOLOGY REVIEWS, 2005, 69 (01) :124-+
[8]  
Demetrakopoulos G E, 1978, World Rev Nutr Diet, V32, P96
[9]   The maize primary cell wall microfibril: A new model derived from direct visualization [J].
Ding, SY ;
Himmel, ME .
JOURNAL OF AGRICULTURAL AND FOOD CHEMISTRY, 2006, 54 (03) :597-606
[10]   Process and economic analysis of pretreatment technologies [J].
Eggeman, T ;
Elander, RT .
BIORESOURCE TECHNOLOGY, 2005, 96 (18) :2019-2025