Co-production bioethanol and xylooligosaccharides from sugarcane bagasse via autohydrolysis pretreatment

被引:47
|
作者
Zhang, Weiwei [1 ]
Zhang, Xiankun [1 ]
Lei, Fuhou [2 ]
Jiang, Jianxin [1 ]
机构
[1] Beijing Forestry Univ, Dept Chem & Chem Engn, MOE Engn Res Ctr Forestry Biomass Mat & Bioenergy, Natl Forest & Grass Adm,Woody Spices East China E, Beijing 100083, Peoples R China
[2] Guangxi Univ Nationalities, Coll Chem & Chem Engn, GuangXi Key Lab Chem, Engn Forest Prod, Nanning 530006, Peoples R China
基金
国家重点研发计划;
关键词
Cellulose; Hemicellulose; saccharification and fermentation; Buffer; Non-ionic surfactants; High lignin content; ENZYMATIC-HYDROLYSIS; SIMULTANEOUS SACCHARIFICATION; ETHANOL-PRODUCTION; LIGNIN; FERMENTATION; LIGNOCELLULOSE; DIGESTIBILITY; ENHANCEMENT; PRODUCTS; RESIDUES;
D O I
10.1016/j.renene.2020.10.034
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Autohydrolysis pretreatment is an effective, commercial and environmentally friendly processes for the co-production of bioethanol and xylooligosaccharides (XOS) from sugarcane bagasse (SCB). An XOS yield of 50.53% was obtained at 200 degrees C for 10 min by autohydrolysis pretreatment, most of cellulose and lignin remained in the solid residues, which can be converted into bioethanol. The ethanol yield (66.67%) in sodium acetate buffer solution (SAAB, pH 5.5) system was higher than that in the deionized water (DW) system (51.88%), because the stable pH regulated by the buffer was beneficial to maintain the cellulase and yeast activity. Moreover, the addition of non-ionic surfactants can effectively promote fermentation performances, especially with Tween 80, 82.28% ethanol yield (of the theoretical) was reached. The use of the buffer system and non-ionic surfactants provides an ideal strategy for ethanol production by fermentation of substrates with high lignin content. Therefore, this study shows a suitable and sustainable process for bioethanol and XOS production from SCB using autohydrolysis pretreatment as onestep of a biorefinery. (c) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2297 / 2305
页数:9
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