Dual assistance of surfactants in glycerol organosolv pretreatment and enzymatic hydrolysis of lignocellulosic biomass for bioethanol production

被引:11
|
作者
Song, Guojie [1 ]
Sun, Chihe [1 ]
Madadi, Meysam [1 ]
Dou, Shaohua [2 ]
Yan, Junshu [3 ]
Huan, Hailin [3 ]
Aghbashlo, Mortaza [4 ]
Tabatabaei, Meisam [5 ,6 ]
Sun, Fubao [1 ]
Ashori, Alireza [7 ]
机构
[1] Jiangnan Univ, Sch Biotechnol, Key Lab Ind Biotechnol, Minist Educ, Wuxi 214122, Peoples R China
[2] Dalian Univ, Coll Life & Hlth, Dalian 116622, Peoples R China
[3] Jiangsu Acad Agr Sci, Inst Anim Sci, Nanjing 210014, Peoples R China
[4] Univ Tehran, Coll Agr & Nat Resources, Fac Agr Engn & Technol, Dept Mech Engn Agr Machinery, Karaj, Iran
[5] Univ Malaysia Terengganu, Higher Inst Ctr Excellence HICoE, Inst Trop Aquaculture & Fisheries AKUATROP, Kuala Nerus 21030, Terengganu, Malaysia
[6] Saveetha Inst Med & Tech Sci, Saveetha Dent Coll, Dept Biomat, Chennai 600077, India
[7] Iranian Res Org Sci & Technol, Dept Chem Technol, Tehran, Iran
基金
中国国家自然科学基金;
关键词
Sugarcane bagasse; Surfactant-assisted pretreatment; High-solid enzymatic hydrolysis; Cellulosic ethanol; Economic analysis; ETHANOL-PRODUCTION; DILUTE-ACID; WHEAT-STRAW; HIGH-SOLIDS; SACCHARIFICATION; FERMENTATION; ECONOMICS; ASPEN;
D O I
10.1016/j.biortech.2024.130358
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
This study investigated an innovative strategy of incorporating surfactants into alkaline-catalyzed glycerol pretreatment and enzymatic hydrolysis to improve lignocellulosic biomass (LCB) conversion efficiency. Results revealed that adding 40 mg/g PEG 4000 to the pretreatment at 195 degrees C obtained the highest glucose yield (84.6%). This yield was comparable to that achieved without surfactants at a higher temperature (240 degrees C), indicating a reduction of 18.8% in the required heat input. Subsequently, Triton X-100 addition during enzymatic hydrolysis of PEG 4000-assisted pretreated substrate increased glucose yields to 92.1% at 6 FPU/g enzyme loading. High-solid fed-batch semi-simultaneous saccharification and co-fermentation using this dual surfactant strategy gave 56.4 g/L ethanol and a positive net energy gain of 1.4 MJ/kg. Significantly, dual assistance with surfactants rendered 56.3% enzyme cost savings compared to controls without surfactants. Therefore, the proposed surfactant dual -assisted promising approach opens the gateway to economically viable enzymemediated LCB biorefinery.
引用
收藏
页数:12
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