Li Chong, Gao Shi, Li Xiaotong, Yang Xiaofeng, Lin Carol Sze Ki
1School of Energy and Environment, City University of Hong Kong, Tat Chee Avenue, Kowloon, Hong Kong.
2Agricultural Genomic Institute at Shenzhen, Chinese Academy of Agricultural Sciences, Shenzhen, 518120 Guangdong People's Republic of China.
Biotechnol Biofuels. 2018 Aug 30;11:236. doi: 10.1186/s13068-018-1233-6. eCollection 2018.
Alkali used for pH control during fermentation and acidification for downstream recovery of succinic acid (SA) are the two largest cost contributors for bio-based SA production. To promote the commercialization process of fermentative SA, the development of industrially important microorganisms that can tolerate low pH has emerged as a crucial issue.
In this study, an in situ fibrous bed bioreactor (isFBB) was employed for the metabolic evolution for selection of strain that can produce SA at low pH using glucose-based medium. An evolved strain named PSA3.0 that could produce SA with a titer of 19.3 g/L, productivity of 0.52 g/L/h, and yield of 0.29 g/g at pH 3.0 from YPD was achieved. The enzyme activity analysis demonstrated that the pathway from pyruvate to acetate was partially blocked in PSA3.0 after the evolution, which is beneficial to cell growth and SA production at low pH. When free-cell batch fermentations were performed using the parent and evolved strains separately, the evolved strain PSA3.0 produced 18.4 g/L SA with a yield of 0.23 g/g at pH 3.0. Although these values were lower than that obtained by the parent strain PSA02004 at its optimal pH 6.0, which were 25.2 g/L and 0.31 g/g, respectively, they were 4.8 and 4.6 times higher than that achieved by PSA02004 at pH 3.0. By fed-batch fermentation, the resultant SA titer of 76.8 g/L was obtained, which is the highest value that ever achieved from glucose-based medium at low pH, to date. When using mixed food waste (MFW) hydrolysate as substrate, 18.9 g/L SA was produced with an SA yield of 0.38 g/g, which demonstrates the feasibility of using low-cost glucose-based hydrolysate for SA production by in a low-pH environment.
This study presents an effective and efficient strategy for the evolution of for SA production under low-pH condition for the first time. The isFBB was demonstrated to improve the metabolic evolution efficiency of to the acidic condition. Moreover, the acetate accumulation was found to be the major reason for the inhibition of SA production at low pH by , which suggested the direction for further metabolic modification of the strain for improved SA production. Furthermore, the evolved strain PSA3.0 was demonstrated to utilize glucose-rich hydrolysate from MFW for fermentative SA production at low pH. Similarly, PSA3.0 is expected to utilize the glucose-rich hydrolysate generated from other carbohydrate-rich waste streams for SA production. This study paves the way for the commercialization of bio-based SA and contributes to the sustainable development of a green economy.
在发酵过程中用于控制pH值的碱以及用于下游琥珀酸(SA)回收的酸化是生物基SA生产中两个最大的成本因素。为推动发酵法SA的商业化进程,开发能够耐受低pH值的具有工业重要性的微生物已成为一个关键问题。
在本研究中,采用原位纤维床生物反应器(isFBB)进行代谢进化,以筛选能够在基于葡萄糖的培养基中于低pH值下生产SA的菌株。获得了一株名为PSA3.0的进化菌株,该菌株在pH 3.0的YPD培养基中能够产生19.3 g/L的SA,生产速率为0.52 g/L/h,产率为0.29 g/g。酶活性分析表明,进化后的PSA3.0中从丙酮酸到乙酸的途径部分受阻,这有利于细胞在低pH值下的生长和SA的生产。当分别使用亲本菌株和进化菌株进行游离细胞分批发酵时,进化菌株PSA3.0在pH 3.0时产生了18.4 g/L的SA,产率为0.23 g/g。尽管这些值低于亲本菌株PSA02004在其最佳pH 6.0时获得的值,分别为25.2 g/L和0.31 g/g,但它们分别是PSA02004在pH 3.0时产率的4.8倍和4.6倍。通过补料分批发酵,获得了76.8 g/L的SA产量,这是迄今为止在低pH值下基于葡萄糖的培养基中所达到的最高值。当使用混合食物垃圾(MFW)水解物作为底物时,产生了18.9 g/L的SA,SA产率为0.38 g/g,这证明了在低pH环境中使用低成本的基于葡萄糖的水解物生产SA的可行性。
本研究首次提出了一种在低pH条件下进化用于SA生产的有效且高效的策略。isFBB被证明可提高对酸性条件的代谢进化效率。此外,发现乙酸积累是低pH值下抑制SA生产的主要原因,这为进一步对该菌株进行代谢改造以提高SA产量指明了方向。此外,进化菌株PSA3.0被证明可利用MFW中富含葡萄糖的水解物在低pH值下进行发酵生产SA。同样,PSA3.0有望利用其他富含碳水化合物的废物流产生的富含葡萄糖的水解物生产SA。本研究为生物基SA的商业化铺平了道路,并为绿色经济的可持续发展做出了贡献。