Alkali pretreated corn stalk combined with enzyme cocktail at low cellulase dosage for the high-titer L-lactic acid production

High cellulase cost is the major barrier to the commercialization of L-lactic acid (L-LA) production from abundant lignocellulosic biomass. In current work, an enzyme cocktail that consisted of the commercial cellulase and the additives was prepared to generate the mono-sugars from the alkali pretreated corn stalk for high concentration L-LA fermentation. A statistical mixture design approach was employed to clarify the synergistic effect of the key components in the cellulase cocktail on mono-sugars production. Based on the optimized proportion (8 mg/g xylanase, 8 mg/g laccase, 0.6 mg/g of LiCl, 12.0 mg/g of Tween80 and 13.6 mg/g of bovine serum albumin (BSA) mixed with the base cellulase) of the enzyme cocktail, fed-batch saccharification was conducted with extreme-low base cellulase (4 FPU/g pulp) loading, and allowing 171.8 g/L of mono-sugars production from 22 % (w/v) of the corn stalk pulp. A maximized 129.4 g/L of L-LA production with 0.917 g/g (total mono-sugars) of yield were realized in the following fermentation using the corn stover hydrolysate. • Cellulase dosage was reduced by mixed with additives and accessory enzymes. • Statistical mixture design was employed to optimize the additives loading in enzyme cocktail. • 171.8 g/L of sugars was obtained from 22 % (w/v) pulp with 4 FPU cellulase/g (substrate) loading. • 129.4 g/L of L-LA with a yield of 0.917 g/g (sugars) was obtained by fermentation.

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Publication Details

Journal
Industrial Crops and Products
Published
2024-12-20
DOI
https://doi.org/10.1016/j.indcrop.2024.120332
Citations
8
Primary Topic
Biofuel production and bioconversion
Type
article
Field-Weighted Citation Impact
1.48

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article

Alkali pretreated corn stalk combined with enzyme cocktail at low cellulase dosage for the high-titer L-lactic acid production

Changsheng Su, Di Cai, Peiyong Qin, Haoran Bi et al.
8 citations
Industrial Crops and Products
Biofuel production and bioconversion
1.48
article

Alkali pretreated corn stalk combined with enzyme cocktail at low cellulase dosage for the high-titer L-lactic acid production

Changsheng Su, Di Cai, Peiyong Qin, Haoran Bi, Yilu Wu, Yong Wang, Changwei Zhang, Liheng Deng, Jiaming Wu, Bin Wang
article en
8 citations

Abstract

High cellulase cost is the major barrier to the commercialization of L-lactic acid (L-LA) production from abundant lignocellulosic biomass. In current work, an enzyme cocktail that consisted of the commercial cellulase and the additives was prepared to generate the mono-sugars from the alkali pretreated corn stalk for high concentration L-LA fermentation. A statistical mixture design approach was employed to clarify the synergistic effect of the key components in the cellulase cocktail on mono-sugars production. Based on the optimized proportion (8 mg/g xylanase, 8 mg/g laccase, 0.6 mg/g of LiCl, 12.0 mg/g of Tween80 and 13.6 mg/g of bovine serum albumin (BSA) mixed with the base cellulase) of the enzyme cocktail, fed-batch saccharification was conducted with extreme-low base cellulase (4 FPU/g pulp) loading, and allowing 171.8 g/L of mono-sugars production from 22 % (w/v) of the corn stalk pulp. A maximized 129.4 g/L of L-LA production with 0.917 g/g (total mono-sugars) of yield were realized in the following fermentation using the corn stover hydrolysate. • Cellulase dosage was reduced by mixed with additives and accessory enzymes. • Statistical mixture design was employed to optimize the additives loading in enzyme cocktail. • 171.8 g/L of sugars was obtained from 22 % (w/v) pulp with 4 FPU cellulase/g (substrate) loading. • 129.4 g/L of L-LA with a yield of 0.917 g/g (sugars) was obtained by fermentation.

Industrial Crops and ProductsVol. 224
Hebei University of Science and Technology (CN), Qinhuangdao Science and Technology Bureau (CN), Beijing University of Chemical Technology (CN)
National Key Research and Development Program of China
Zero hunger
Openalex Percentile: Top 19%
Biofuel production and bioconversion
1.48
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