Deng Pan, Chen Lijie, Xin Chengxun, Bai Fengwu
School of Life Science and Biotechnology, Dalian University of Technology, Dalian 116024, China.
Sheng Wu Gong Cheng Xue Bao. 2011 Oct;27(10):1448-56.
A mixture of fructose and glucose was developed to simulate the hydrolysate of Jerusalem artichoke tubers, the fructose-based feedstock suitable for butanol production. With the initial pH of 5.5 without regulation during mixed-sugar fermentation, as high as 23.26 g/L sugars were remained unconverted, and butanol production of 5.51 g/L were obtained. Compared with either glucose or fructose fermentation, the early termination of mixed-sugar fermentation might be caused by toxic organic acids and the low pH. When the pH of the fermentation system was controlled at higher levels, it was found that sugars utilization was facilitated, but less butanol was produced due to the over-accumulation of organic acids. On the other hand, when the pH was controlled at lower levels, more sugars were remained unconverted, although butanol production was improved. Based on these experimental results, a stage-wise pH regulation strategy, e.g., controlling the pH of the fermentation system at 5.5 untill the OD620 reached 1.0, and then the pH control was removed, was developed, which significantly improved the fermentation performance of the system, with only 2.05 g/L sugars unconverted and 10.48 g/L butanol produced.
开发了一种果糖和葡萄糖的混合物来模拟菊芋块茎的水解产物,菊芋块茎是适合丁醇生产的基于果糖的原料。在混合糖发酵过程中初始pH为5.5且不进行调节的情况下,高达23.26 g/L的糖未被转化,丁醇产量为5.51 g/L。与葡萄糖或果糖发酵相比,混合糖发酵的提前终止可能是由有毒有机酸和低pH值导致的。当发酵系统的pH控制在较高水平时,发现糖的利用率得到促进,但由于有机酸的过度积累,丁醇产量较低。另一方面,当pH控制在较低水平时,尽管丁醇产量有所提高,但更多的糖未被转化。基于这些实验结果,制定了一种分段pH调节策略,例如,将发酵系统的pH控制在5.5直到OD620达到1.0,然后取消pH控制,这显著提高了系统的发酵性能,只有2.05 g/L的糖未被转化,丁醇产量为10.48 g/L。