对面包酵母的海藻糖积累条件及补料分批发酵进行了研究。
Trehalose accumulation condition in baker's yeast was studied in fed batch fermentation.
通过与实际发酵过程比较,较好地反映了谷氨酸补料分批发酵过程。
By comparing the practical ferment process, the obtained fitted model could reflect the fermentation process of L-glutamic acid fed-batch appropriately.
以分批发酵最优条件为依据,对菌株sw0370进行了补料分批发酵研究。
Fed batch fermentation was studied with SW0370 according to the optimum condition of batch fermentation.
以分批发酵最优条件为依据,对菌株tv2564进行了补料分批发酵研摘要究。
Fed batch fermentation was studied with TV2564 according to the optimum condition of batch fermentation.
在此基础上建立了生物转化合成FDP的补料分批操作方式,以产品成本最低为目标优化了反应操作时间。
Then, the fed-batch operation strategy was formulated for FDP production, and the operation time was optimized with the production cost as a main concern.
实验还表明,分批补料培养可以提高菌体浓度,可使转硒效率和绝对量增加。
We also found that the fed-batch can enhance the concentration of thalli and increase the efficiency and the absolute value of transferring se.
在高密度发酵过程中,会产生一些有害抑制代谢副产物,但通过分批补料可以降低影响。
During the high density fermentation, some toxic inhibitor metabolites produced, which could be decreased by fed-batch culture.
结果表明:通过分批补料对酶产率有提高,以高酯果胶为底物酶产率提高7.0 % ,以低酯果胶为底物酶产率提高2 3.5 % ;
The results showed that to feed batch culture can enhance enzyme productivity by 7.0 % with high methoxyl pectin as substrate, and by 2 3.5 % with low methoxyl pectin as substrate.
然后在该培养基配方的基础上进行摇瓶分批补料发酵试验,确定最佳补料方案。
The fed-batch fermentation method was studied by flask culture based on the optimal medium.
采用分批补料的供糖方式的发酵可将原料利用率从82.62%提高到88.51%。
Utilization ratio on raw material could increase from 82.62% to 88.51% in fed-batch fermentation.
本文研究了玉米皮水解液发酵生产饲料酵母的摇瓶间歇培养和分批补料培养条件,进行了10L反应器分批补料培养试验。
The biotechnology of flask batch and fed-batch culture to produce yeast from cornhusk hydrolysate was studied and the fed -batch process in 10L bioreactor was conducted.
本文研究了玉米皮水解液发酵生产饲料酵母的摇瓶间歇培养和分批补料培养条件,进行了10L反应器分批补料培养试验。
The biotechnology of flask batch and fed-batch culture to produce yeast from cornhusk hydrolysate was studied and the fed -batch process in 10L bioreactor was conducted.
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