State Key Laboratory of Materials-Oriented Chemical Engineering, College of Biotechnology and Pharmaceutical Engineering, Nanjing University of Technology, No. 5 Xinmofan Road, Nanjing, 210009, People's Republic of China.
Appl Biochem Biotechnol. 2011 Apr;163(8):946-53. doi: 10.1007/s12010-010-9098-6. Epub 2010 Oct 13.
Substrate concentration in 2,3-butanediol (2,3-BD) fermentation could not be controlled well in traditional feeding strategies, such as constant, impulse, and exponential feeding strategies. In the present study, fermentative 2,3-BD production by Klebsiella oxytoca was investigated under different batch and fed-batch strategies. The glucose-feedback fed-batch strategy was proved to be not effective for economical 2,3-BD production for the inability of timely feeding, leading that the bacteria reused 2,3-BD as carbon source for cell growth. Based on the phenomena that the byproducing acids caused the pH declining and the requirement of maintaining the pH at a proper level for both cell growth and 2,3-BD accumulation, an improved strategy of pH-stat fed-batch culture with glucose and sodium hydrate fed at the same time was established. Thus, the residual glucose concentration could be controlled through the adjustment of pH automatically. At last, efficient 2,3-BD production was fulfilled under this fed-batch strategy, and the highest 2,3-BD concentration, productivity, and yield were 127.9 g/l, 1.78 g/(l•h), and 0.48 g/g (2,3-BD/glucose), respectively, compared to 98.5 g/l, 1.37 g/(l•h), and 0.43 g/g obtained in glucose-feedback fed-batch strategy. This feeding strategy was simple and easy to operate and could be feasible for industrial 2,3-BD production in the future.
在传统的补料策略(如恒速、脉冲和指数补料策略)中,2,3-丁二醇(2,3-BD)发酵中的底物浓度无法得到很好的控制。在本研究中,研究了在不同批次和补料分批策略下,氧化葡萄糖酸杆菌发酵生产 2,3-BD。葡萄糖反馈补料分批策略对于经济高效的 2,3-BD 生产并不有效,因为无法及时补料,导致细菌将 2,3-BD 重新用作细胞生长的碳源。基于副产物酸导致 pH 下降以及细胞生长和 2,3-BD 积累都需要维持适当 pH 水平的现象,建立了一种同时补加葡萄糖和氢氧化钠的 pH -stat 补料分批培养的改进策略。因此,可以通过自动调整 pH 值来控制残余葡萄糖浓度。最后,在这种补料分批策略下实现了高效的 2,3-BD 生产,最高 2,3-BD 浓度、生产率和产率分别达到 127.9 g/l、1.78 g/(l•h)和 0.48 g/g(2,3-BD/葡萄糖),而葡萄糖反馈补料分批策略下分别为 98.5 g/l、1.37 g/(l•h)和 0.43 g/g。这种补料策略简单易行,将来有望在工业 2,3-BD 生产中得到应用。