Ryu H W, Hahn S K, Chang Y K, Chang H N
BioProcess Engineering Research Center and Department of Chemical Engineering, KAIST, 373-1, Kusong-dong, Yusong-gu, Taejon, 305-701, Korea.
Biotechnol Bioeng. 1997 Jul 5;55(1):28-32. doi: 10.1002/(SICI)1097-0290(19970705)55:1<28::AID-BIT4>3.0.CO;2-Z.
High cell density fed-batch fermentation of Alcaligenes eutrophus was carried out for the production of poly(3-hydroxybutyrate) (PHB) in a 60-L fermentor. During the fermentation, pH was controlled with NH(4)OH solution and PHB accumulation was induced by phosphate limitation instead of nitrogen limitation. The glucose feeding was controlled by monitoring dissolved oxygen (DO) concentration and glucose concentration in the culture broth. The glucose concentration fluctuated within the range of 0-20 g/L. We have investigated the effect of initial phosphate concentration on the PHB production when the initial volume was fixed. Using an initial phosphate concentration of 5.5 g/L, the fed-batch fermentation resulted in a final cell concentration of 281 g/L, a PHB concentration of 232 g/L, and a PHB productivity of 3.14 g/L . h, which are the highest values ever reported to date. In this case, PHB content, cell yield from glucose, and PHB yield from glucose were 80, 0.46, and 0.38% (w/w), respectively.
在60升发酵罐中进行了产碱杆菌的高细胞密度补料分批发酵以生产聚(3-羟基丁酸酯)(PHB)。发酵过程中,用NH₄OH溶液控制pH值,通过磷酸盐限制而非氮限制诱导PHB积累。通过监测培养液中的溶解氧(DO)浓度和葡萄糖浓度来控制葡萄糖补料。葡萄糖浓度在0 - 20克/升范围内波动。当初始体积固定时,我们研究了初始磷酸盐浓度对PHB产量的影响。使用5.5克/升的初始磷酸盐浓度,补料分批发酵得到的最终细胞浓度为281克/升,PHB浓度为232克/升,PHB生产率为3.14克/升·小时,这些都是迄今为止报道的最高值。在这种情况下,PHB含量、葡萄糖的细胞得率和葡萄糖的PHB得率分别为80%、0.46和0.38%(w/w)。