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Utilization of lignocellulosic hydrolysate for succinate fermentation. (A) Preparation process of corn stover hydrolysate including pretreatment, enzymatic hydrolysis, detoxification, and sugar composition analysis; (B–C) Fermentation of ESC6 crp -W68 + in <t>a</t> <t>5-L</t> bioreactor using synthetic sugar mixtures mimicking hydrolysate composition (B) and actual corn stover hydrolysate (C) as carbon sources. All experimental data were performed in triplicate, and error bars represent the standard deviation.
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Utilization of lignocellulosic hydrolysate for succinate fermentation. (A) Preparation process of corn stover hydrolysate including pretreatment, enzymatic hydrolysis, detoxification, and sugar composition analysis; (B–C) Fermentation of ESC6 crp -W68 + in a 5-L bioreactor using synthetic sugar mixtures mimicking hydrolysate composition (B) and actual corn stover hydrolysate (C) as carbon sources. All experimental data were performed in triplicate, and error bars represent the standard deviation.

Journal: Synthetic and Systems Biotechnology

Article Title: Engineering Escherichia coli for robust Co-utilization of glucose and xylose enables high-titer succinate production from lignocellulosic hydrolysates

doi: 10.1016/j.synbio.2026.01.006

Figure Lengend Snippet: Utilization of lignocellulosic hydrolysate for succinate fermentation. (A) Preparation process of corn stover hydrolysate including pretreatment, enzymatic hydrolysis, detoxification, and sugar composition analysis; (B–C) Fermentation of ESC6 crp -W68 + in a 5-L bioreactor using synthetic sugar mixtures mimicking hydrolysate composition (B) and actual corn stover hydrolysate (C) as carbon sources. All experimental data were performed in triplicate, and error bars represent the standard deviation.

Article Snippet: For fermentation, the seed culture was inoculated into a 5-L bioreactor (Shanghai Baoxing Bio-Engineering Equipment, Shanghai, China) at a 10 % (v/v) inoculum ratio, with the bioreactor having a working volume of 2 L. During the aerobic growth phase, the air flow rate was maintained at 2 L/min, the agitator speed was controlled between 300 and 550 rpm, the dissolved oxygen level was sustained above 60 %, the temperature was regulated at 37 °C, and the pH was maintained at 6.8 via the addition of 15 % ammonia solution.

Techniques: Standard Deviation