Li Fan, Ge Xumeng, Li Ning, Bai Fengwu
Department of Bioscience and Bioengineering, Dalian University of Technology, Dalian 116023, China.
Sheng Wu Gong Cheng Xue Bao. 2009 Sep;25(9):1329-37.
In order to save energy consumption for the downstream processes, consecutive very-high-gravity batch fermentation was developed for ethanol production with the self-flocculating yeast Saccharomyces cerevisiae flo. The fermentation system exhibited a high ethanol productivity of 8.2 g/(L x h) with average ethanol concentration around 120 g/L. However, deterioration of the sedimentation performance of yeast flocs was observed as the consecutive fermentation process was prolonged, which significantly extended the time required for yeast flocs to separate from fermentation broth, and exaggerated the inhibition of high ethanol concentration on the yeast flocs, making them quickly lost viability and the fermentation system interrupted after 11 consecutive batches. Experimental results illustrated that decrease of the size of yeast flocs was the main reason, which could be prevented by stimulating the propagation of the yeast flocs. Thus, yeast was purged from the fermentation system at the end of each batch, and the concentration of yeast flocs within the fermentor was maintained at a relatively low level to stimulate their propagation. Although the ethanol productivity was decreased to 4.0 g/(L x h), the size of yeast flocs was stabilized after 10 consecutive batches and maintained for another 14 batches without further decrease, indicating the fermentation system could be operated reliably.
为了降低下游工艺的能耗,开发了连续超高浓度分批发酵法,用于利用自絮凝酵母酿酒酵母flo生产乙醇。该发酵系统表现出8.2 g/(L·h)的高乙醇生产率,平均乙醇浓度约为120 g/L。然而,随着连续发酵过程的延长,观察到酵母絮凝物的沉降性能变差,这显著延长了酵母絮凝物与发酵液分离所需的时间,并加剧了高乙醇浓度对酵母絮凝物的抑制作用,导致它们迅速失去活力,连续11批发酵后发酵系统中断。实验结果表明,酵母絮凝物尺寸减小是主要原因,通过刺激酵母絮凝物的繁殖可以防止这种情况。因此,在每批发酵结束时从发酵系统中排出酵母,并将发酵罐内酵母絮凝物的浓度维持在相对较低的水平以刺激其繁殖。尽管乙醇生产率降至4.0 g/(L·h),但酵母絮凝物的尺寸在连续10批发酵后稳定下来,并在接下来的14批发酵中保持稳定,不再减小,这表明发酵系统可以可靠运行。