Eco-friendly consolidated process for co-production of xylooligosaccharides and fermentable sugars using self-providing xylonic acid as key pretreatment catalyst

被引:54
作者
Zhou, Xin [1 ,2 ,3 ]
Xu, Yong [1 ,2 ,3 ]
机构
[1] Nanjing Forestry Univ, Minist Educ, Key Lab Forestry Genet & Biotechnol, Nanjing 210037, Peoples R China
[2] Nanjing Forestry Univ, Jiangsu Coinnovat Ctr Efficient Proc & Utilizat F, Nanjing 210037, Peoples R China
[3] Nanjing Forestry Univ, Coll Chem Engn, 159 Longpan Rd, Nanjing 210037, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
Xylooligosaccharides; Xylonic acid; Xylose; Sugarcane bagasse; Enzymatic hydrolysis; DILUTE-ACID; ENZYMATIC-HYDROLYSIS; CORN STOVER; CELLULOSE; BAGASSE; LIGNIN; COMBINATION; OLIGOSACCHARIDES; HEMICELLULOSES; OPTIMIZATION;
D O I
10.1186/s13068-019-1614-5
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Background: Obtaining high-value products from lignocellulosic biomass is central for the realization of industrial biorefinery. Acid pretreatment has been reported to yield xylooligosaccharides (XOS) and improve enzymatic hydrolysis. Moreover, xylose, an inevitable byproduct, can be upgraded to xylonic acid (XA). The aim of this study was to valorize sugarcane bagasse (SB) by starting with XA pretreatment for XOS and glucose production within a multiproduct biorefinery framework. Results: SB was primarily subjected to XA pretreatment to maximize the XOS yield by the response surface method (RSM). A maximum XOS yield of 44.5% was achieved by acid pretreatment using 0.64 M XA for 42 min at 154 degrees C. Furthermore, XA pretreatment can efficiently improve enzymatic digestibility, and achieved a 90.8% cellulose conversion. In addition, xylose, the inevitable byproduct of the acid-hydrolysis of xylan, can be completely converted to XA via bio-oxidation of Gluconobacter oxydans (G. oxydans). Subsequently, XA and XOS can be simultaneously separated by electrodialysis. Conclusions: XA pretreatment was explored and exhibited a promising ability to depolymerize xylan into XOS. Mass balance analysis showed that the maximum XOS and fermentable sugars yields reached 10.5 g and 30.9 g per 100 g raw SB, respectively. In summary, by concurrently producing XOS and fermentable sugars with high yields, SB was thus valorized as a promising feedstock of lignocellulosic biorefinery for value-added products.
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页数:10
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