Wu Youduo, Bai Yidi, Zhang Daojing, Cheng Chi, Chen Lijie, Bai Fengwu, Xue Chuang
1School of Bioengineering, Dalian University of Technology, No 2 Linggong Road, Dalian, 116024 China.
2State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai, 200237 China.
Biotechnol Biofuels. 2019 Nov 7;12:264. doi: 10.1186/s13068-019-1604-7. eCollection 2019.
Corn stover (CS) is evaluated as the most favorable candidate feedstock for butanol production via microbial acetone-butanol-ethanol (ABE) fermentation by . By independent acid pretreatment and enzymatic hydrolysis, fermentable sugars (mainly glucose and xylose) were released, of which glucose was naturally utilized as the most preferred carbon source by . However, the ABE fermentation using corn stover hydrolysate (CSH) without detoxification is typically limited to poor sugars utilization, butanol production and productivity. In the presence of pretreatment-derived inhibitors, the intracellular ATP and NADH, as important factors involved in cell growth, solventogenesis initiation and stress response, are exceedingly challenged owing to disrupted glucose phosphotransferase system (PTS). Therefore, there is a necessity to develop effective engineering approaches to overcome these limitations for high-efficient butanol production from CSH without detoxification.
PTS-engineered strains were constructed via overexpression and knockout of gene encoding glucose-specific PTS IICBA, which pleiotropically regulated glucose utilization, cell growth, solventogenesis and inhibitors tolerance. The PTS-overexpressing strain exhibited high fermentation efficiency, wherein butanol production and productivity was 11.1 g/L and 0.31 g/L/h, compared to those of 11.0 g/L and 0.15 g/L/h with the PTS-deficient strain. During CSH culture without detoxification, the PTS-overexpressing strain exhibited desirable inhibitors tolerance and solventogenesis with butanol production of 10.0 g/L, increased by 300% and 400% compared to those of 2.5 and 2.0 g/L with the control and PTS-deficient strains, respectively. As a result of extra glucose and 10 g/L CaCO addition into CSH, butanol production and productivity were further maximized to 12.5 g/L and 0.39 g/L/h. These validated improvements on the PTS-overexpressing strain were ascribed to not only efficient glucose transport but also its cascading effects on intracellular ATP and NADH generation, solventogenesis initiation and inhibitors tolerance at the exponential growth phase.
The PTS regulation could be an effective engineering approach for high-efficient ABE fermentation from lignocellulosic hydrolysates without detoxification or wastewater generation, providing fundamental information for economically sustainable butanol production with high productivity.
玉米秸秆(CS)被认为是通过微生物丙酮 - 丁醇 - 乙醇(ABE)发酵生产丁醇的最有利候选原料。通过独立的酸预处理和酶水解,可释放出可发酵糖(主要是葡萄糖和木糖),其中葡萄糖是被自然用作最优选碳源的。然而,使用未经解毒的玉米秸秆水解物(CSH)进行ABE发酵通常受到糖利用率低、丁醇产量和生产率的限制。在存在预处理衍生抑制剂的情况下,细胞内的ATP和NADH作为参与细胞生长、溶剂生成起始和应激反应的重要因素,由于葡萄糖磷酸转移酶系统(PTS)的破坏而受到极大挑战。因此,有必要开发有效的工程方法来克服这些限制,以便从未经解毒的CSH中高效生产丁醇。
通过过表达和敲除编码葡萄糖特异性PTS IICBA的基因构建了PTS工程化的菌株,该基因多效性地调节葡萄糖利用、细胞生长、溶剂生成和抑制剂耐受性。过表达PTS的菌株表现出高发酵效率,其中丁醇产量和生产率分别为11.1 g/L和0.31 g/L/h,而PTS缺陷菌株的丁醇产量和生产率分别为11.0 g/L和0.15 g/L/h。在未经解毒的CSH培养过程中,过表达PTS的菌株表现出良好的抑制剂耐受性和溶剂生成能力,丁醇产量为10.0 g/L,与对照菌株和PTS缺陷菌株分别为2.5 g/L和2.0 g/L相比,产量分别提高了300%和400%。由于向CSH中额外添加了葡萄糖和10 g/L碳酸钙,丁醇产量和生产率进一步最大化至12.5 g/L和0.39 g/L/h。对过表达PTS菌株的这些验证改进不仅归因于有效的葡萄糖转运,还归因于其在指数生长期对细胞内ATP和NADH生成、溶剂生成起始和抑制剂耐受性的级联效应。
PTS调节可能是一种有效的工程方法,用于从木质纤维素水解物中进行高效的ABE发酵,无需解毒或产生废水,为经济可持续的高生产率丁醇生产提供了基础信息。