Alkali-oxygen treatment prior to the mechanical pulping of hardwood enhances enzymatic hydrolysis and carbohydrate recovery through selective lignin modification

被引:40
作者
Wu, Jie [1 ]
Chandra, Richard [1 ]
Saddler, Jack [1 ]
机构
[1] Univ British Columbia, Fac Forestry, Dept Wood Sci, Forest Prod Biotechnol Bioenergy Grp, 2424 Main Mall, Vancouver, BC V6T 1Z4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
STEAM PRETREATED SOFTWOOD; CELLULOSE; SACCHARIFICATION; DELIGNIFICATION; HEMICELLULOSE; TECHNOLOGIES; CELLULASES; ENZYMES; POPLAR; WOOD;
D O I
10.1039/c8se00452h
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Aspen chips were impregnated with sodium carbonate (70 degrees C, overnight) and oxygen (110 degrees C, 2 hours) prior to pre-steaming (190 degrees C, 15 min) and mechanical refining. This pretreatment protocol resulted in the removal of 44% of the lignin while retaining 55% of the hemicellulose (which was enriched with carboxylic acid groups (78 mmol kg(-1))) in the water-insoluble fraction. Lignin removal/modification improved fiber swelling and increased cellulose accessibility, resulting in a biomass substrate that could be readily hydrolyzed (80% cellulose hydrolysis, 100% xylan hydrolysis) at an enzyme loading of 20 mg g(-1) cellulose. To further enhance the recovery of the hemicellulose component and the susceptibility of the water-insoluble fraction to enzymatic hydrolysis, a pre-hydrolysis (170 degrees C, 1 hour) step was added prior to alkali-oxygen impregnation. This resulted in a total recovery of 72% of the original hemicellulose from both the solid and liquid fractions. Alternatively, lowering the steaming temperature to 130 degrees C resulted in the preservation of 72% of the hemicellulose in the water insoluble fraction. Although less lignin was removed at the lower, 130 degrees C temperature, the resulting lignin contained a greater amount of acid groups (107 mmol of carboxylic acid groups per kg). Substrates containing lignin which were enriched in acid groups showed increased swelling and a decrease in the tendency of the lignin to bind enzymes through hydrophobic interactions. This substantially reduced the negative effects of lignin on enzymatic hydrolysis.
引用
收藏
页码:227 / 236
页数:10
相关论文
共 66 条
[1]   Pretreatment technologies for an efficient bioethanol production process based on enzymatic hydrolysis: A review [J].
Alvira, P. ;
Tomas-Pejo, E. ;
Ballesteros, M. ;
Negro, M. J. .
BIORESOURCE TECHNOLOGY, 2010, 101 (13) :4851-4861
[2]  
[Anonymous], 1996, HDB PULPING PAPERMAK
[3]   Fundamentals of oxygen delignification. Part II. Functional group formation elimination in residual kraft lignin [J].
Asgari, F ;
Argyropoulos, DS .
CANADIAN JOURNAL OF CHEMISTRY-REVUE CANADIENNE DE CHIMIE, 1998, 76 (11) :1606-1615
[4]  
Bendzalova M, 1996, CELL CHEM TECHNOL, V30, P19
[5]   Weak lignin-rinding enzymes - A novel approach to improve activity of cellulases for hydrolysis of lignocellulosics [J].
Berlin, A ;
Gilkes, N ;
Kurabi, A ;
Bura, R ;
Tu, MB ;
Kilburn, D ;
Saddler, J .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2005, 121 (1-3) :163-170
[6]   Inhibition of cellulase, xylanase and β-glucosidase activities by softwood lignin preparations [J].
Berlin, Alex ;
Balakshin, Mikhail ;
Gilkes, Neil ;
Kadla, John ;
Maximenko, Vera ;
Kubo, Satoshi ;
Saddler, Jack .
JOURNAL OF BIOTECHNOLOGY, 2006, 125 (02) :198-209
[7]   Wet Explosion: a Universal and Efficient Pretreatment Process for Lignocellulosic Biorefineries [J].
Biswas, Rajib ;
Uellendahl, Hinrich ;
Ahring, Birgitte K. .
BIOENERGY RESEARCH, 2015, 8 (03) :1101-1116
[8]   Adsorption and activity profiles of cellulases during the hydrolysis of two Douglas fir pulps [J].
Boussaid, A ;
Saddler, JN .
ENZYME AND MICROBIAL TECHNOLOGY, 1999, 24 (3-4) :138-143
[9]   Enhanced enzymatic hydrolysis of olive tree wood by steam explosion and alkaline peroxide delignification [J].
Cara, C ;
Ruiz, E ;
Ballesteros, I ;
Negro, MJ ;
Castro, E .
PROCESS BIOCHEMISTRY, 2006, 41 (02) :423-429
[10]   Substrate pretreatment: The key to effective enzymatic hydrolysis of lignocellulosics? [J].
Chandra, R. P. ;
Bura, R. ;
Mabee, W. E. ;
Berlin, A. ;
Pan, X. ;
Saddler, J. N. .
BIOFUELS, 2007, 108 :67-93