酵母
发酵
呼吸商
补料分批培养
生物反应器
二氧化碳
糖
产量(工程)
化学
氮气
细胞生长
生物化学
食品科学
有机化学
冶金
材料科学
作者
Xiao Li,Cong Huang,Chaoqun Xu,Ya‐Li Tan,Yudi Luo,Kun Zou,Jianhua Li,Zhangshuang Deng,Zhong Zheng,Han Ye,Xiaolong Zhang,Zheng Nian
摘要
The high cell density culture of baker's yeast FX-2 was investigated in a 50 L(A) automatic bioreactor. Herein, it was found firstly that the Crabtree effect clearly existed in batch fermentation with higher glucose content, then the critical initial glucose content range (≤2.00 g L-1 ) was reasonably ascertained to effectively avoid Crabtree effect. In the next fed-batch fermentations with different strategies, the second strategy (maintain ethanol concentration lower than 0.10% and pH around 4.80) was confirmed to be more beneficial to yeast growth than the first strategy (keep reducing sugar not more than 2.00 g L-1 and control steady Carbon/Nitrogen ratio 3.05:1.00). After that, one optimal control strategy (maintain pH around 4.80 and keep respiratory quotient in the range of 0.90-1.00) was constructed to further enhance cell yield. Under an optimal control strategy, four schemes with the aim of achieving pH-stat were compared, and yeast extract instead of other alkaline materials was selected as a better regulator. As a result, 148.37 g L-1 dry cell weight, 38.25 × 108 mL-1 living cells, and 8.24 g L-1 h-1 productivity were harvested, which respectively elevated 23.74%, 135.38%, and 24.47% compared to that obtained under the traditional scheme (regulate pH with ammonia); meanwhile, the maximum oxygen uptake rate and carbon dioxide excretion rate were both more than 250.00 mmol L-1 min-1 .
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