Enhanced fermentable sugar production in lignocellulosic biorefinery by exploring a novel corn stover and configuring high-solid pretreatment conditions

被引:7
|
作者
Zabed, Hossain M. [1 ,2 ]
Akter, Suely [2 ]
Dar, Mudasir A. [3 ]
Tuly, Jamila A. [2 ]
Aswathi, Mukesh Kumar [4 ]
Yun, Junhua [2 ]
Li, Jia [1 ]
Qi, Xianghui [1 ,2 ]
机构
[1] Guangzhou Univ, Sch Life Sci, Guangzhou 510006, Guangdong, Peoples R China
[2] Jiangsu Univ, Sch Food & Biol Engn, 301 Xuefu Rd, Zhenjiang 212013, Jiangsu, Peoples R China
[3] Jiangsu Univ, Biofuels Inst, Sch Environm & Safety Engn, Zhenjiang 212013, Jiangsu, Peoples R China
[4] Northwest A&F Univ, Coll Nat Resources & Environm, Yangling 712100, Shaanxi, Peoples R China
关键词
Lignocellulosic biomass; Biomass processing; Pretreatment; Biorefinery; Fermentable sugar; DILUTE-ACID PRETREATMENT; SIMULTANEOUS SACCHARIFICATION; ENZYMATIC-HYDROLYSIS; ETHANOL-PRODUCTION; PHOSPHORIC-ACID; BIOMASS; PERFORMANCE; CONVERSION; STALK;
D O I
10.1016/j.biortech.2023.129498
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
This study aimed to produce enhanced fermentable sugars from a novel stover system through the bioprocessing of its soluble sugars and insoluble carbohydrates. The pretreatment conditions were optimized for this high sugar-containing stover (HSS) to control inhibitor formation and obtain enhanced fermentable sugar concentrations. The optimum temperature, acid loading, and reaction time for the pretreatment were 155 degrees C, 0.5%, and 30 min, respectively, providing up to 97.15% sugar yield and 76.51 g/L total sugars at 10% solid-load. Sugar concentration further increased to 126.9 g/L at 20% solid-load, generating 3.89 g/L acetate, 0.92 g/L 5-hydroxymethyl furfural, 0.82 g/L furfural, and 3.75 g/L total phenolics as inhibitors. To determine the effects of soluble sugars in HSS on fermentable sugar yield and inhibitor formation, sugar-removed HSS was further studied under the optimum conditions. Although prior removal of sugars exhibited a reduction in inhibitor generation, it also decreased total fermentable sugar production to 115.45 g/L.
引用
收藏
页数:11
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