Coproduction of xylose, lignosulfonate and ethanol from wheat straw

被引:33
|
作者
Zhu, Shengdong [1 ]
Huang, Wangxiang [1 ]
Huang, Wenjing [1 ]
Wang, Ke [1 ]
Chen, Qiming [1 ]
Wu, Yuanxin [1 ]
机构
[1] Wuhan Inst Technol, Hubei Key Lab Novel Chem Reactor & Green Chem Tec, Sch Chem Engn & Pharm, Key Lab Green Chem Proc,Minist Educ, Wuhan 430073, Peoples R China
基金
中国国家自然科学基金;
关键词
Wheat straw; Xylose; Lignosulfonate; Ethanol; Biorefinery; SULFITE-FORMALDEHYDE PRETREATMENT; ENZYMATIC-HYDROLYSIS; RICE STRAW; FERMENTATION; SACCHARIFICATION; BIOREFINERY; CONVERSION; BIOMASS; LIGNIN; FUTURE;
D O I
10.1016/j.biortech.2015.02.115
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A novel integrated process to coproduce xylose, lignosulfonate and ethanol from wheat straw was investigated. Firstly, wheat straw was treated by dilute sulfuric acid and xylose was recovered from its hydrolyzate. Its optimal conditions were 1.0 wt% sulfuric acid, 10% (w/v) wheat straw loading, 100 degrees C, and 2 h. Then the acid treated wheat straw was treated by sulfomethylation reagent and its hydrolyzate containing lignosulfonate was directly recovered. Its optimal conditions were 150 degrees C, 15% (w/v) acid treated wheat straw loading, and 5 h. Finally, the two-step treated wheat straw was converted to ethanol through enzymatic hydrolysis and microbial fermentation. Under optimal conditions, 1 kg wheat straw could produce 0.225 kg xylose with 95% purity, 4.16 kg hydrolyzate of sulfomethylation treatment containing 5.5% lignosulfonate, 0.183 kg ethanol and 0.05 kg lignin residue. Compared to present technology, this process is a potential economically profitable wheat straw biorefinery. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:234 / 239
页数:6
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