Abstract

BackgroundLignocellulosic biomass has been commonly regarded as a potential feedstock for the production of biofuels and biochemicals. High sugar yields and the complete bioconversion of all the lignocellulosic sugars into valuable products are attractive for the utilization of lignocelluloses. It is essential to pretreat and hydrolyze lignocelluloses at high solids loadings during industrial processes, which is more economical and environmentally friendly as capital cost, energy consumption, and water usage can be reduced. However, oligosaccharides are inevitably released during the high solids loading enzymatic hydrolysis and they are more recalcitrant than monosaccharides for microorganisms.ResultsA fed-batch enzymatic hydrolysis of corn stover pretreated by the sodium hydroxide–methanol solution (SMs) at high solids loading was demonstrated to reach the high concentrations and yields of fermentable sugars. Glucose, xylose, cello-oligosaccharides, and xylo-oligosaccharides achieved 146.7 g/L, 58.7 g/L, 15.6 g/L, and 24.7 g/L, respectively, when the fed-batch hydrolysis was started at 12% (w/v) solids loading, and 7% fresh substrate and a standardized blend of cellulase, β-glucosidase, and hemicellulase were fed consecutively at 3, 6, 24, and 48 h to achieve a final solids loading of 40% (w/v). The total conversion of glucan and xylan reached 89.5% and 88.5%, respectively, when the oligosaccharides were taken into account. Then, a fed-batch culture on the hydrolysates was investigated for lipid production by Cutaneotrichosporon oleaginosum. Biomass, lipid content, and lipid yield were 50.7 g/L, 61.7%, and 0.18 g/g, respectively. The overall consumptions of cello-oligosaccharides and xylo-oligosaccharides reached 74.1% and 68.2%, respectively.ConclusionsHigh sugars concentrations and yields were achieved when the enzyme blend was supplemented simultaneously with the substrate at each time point of feeding during the fed-batch enzymatic hydrolysis. Oligosaccharides were co-utilized with monosaccharides during the fed-batch culture of C. oleaginosum. These results provide a promising strategy to hydrolyze alkaline organosolv-pretreated corn stover into fermentable sugars with high concentrations and yields for microbial lipid production.

Highlights

  • Lignocellulosic biomass has been commonly regarded as a potential feedstock for the production of biofuels and biochemicals

  • Over 70% of lignin was removed by the sodium hydroxide–methanol solution (SMs) pretreatment, which was consistent with the traditional alkaline aqueous solution pretreatment that could dissolve lignin considerably [34]

  • The carbohydrate polymers within lignocelluloses could be well depolymerized into fermentable sugars by the commercial enzyme cocktail, when the hydrolysis was performed at relatively low solids loadings

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Summary

Introduction

Lignocellulosic biomass has been commonly regarded as a potential feedstock for the production of biofuels and biochemicals. Lignocellulosic biomass has already been widely regarded as a potential feedstock for the production of biofuels and biochemicals due to its low cost, abundance, and sustainability [1, 2]. Enzymatic hydrolysis has been predominantly applied for the production of fermentable sugars from lignocelluloses for its high selectivity and mild processing conditions [3]. Various pretreatment techniques have been developed to address biomass recalcitrance by disrupting physical barriers of cell wall, reducing cellulose crystallinity, and removing lignin and hemicellulose, for the purpose of facilitating the enzymatic hydrolysis of lignocelluloses into fermentable sugars [5,6,7]. Alkali pretreatment has attracted extensive attentions, for its capability of preserving a large proportion of cellulose and removing lignin under mild processing conditions [9, 10]

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