Department of Chemical and Biomolecular Engineering, Korea Advanced Institute of Science and Technology, Daejeon 305-701, Korea.
J Microbiol Biotechnol. 2009 Nov;19(11):1369-73.
Succinic acid was produced by continuous fermentation of Actinobacillus succinogenes sp. 130Z in an external membrane cell recycle reactor to improve viable cell concentration and productivity. Using this system, cell concentration increased to 16.4 g/l at the dilution rate 0.2 h-1, up to 3 times higher than that of batch culture, and the volumetric productivity of succinic acid increased up to 6.63 g/l/h at the dilution rate 0.5 h-1, 5 times higher than that of batch fermentation. However, in the continuous culture using a high dilution rate, operational problems including severe membrane fouling and contamination by lactic acid producer were observed. Another succinic acid producer, Mannheimia succiniciproducens MBEL55E, was also utilized in this system, and the cell concentration and productivity of succinic acid at the dilution rate of 0.3 h-1 were found to be above 3 and 2.3 times higher, respectively, compared with those obtained at the dilution rate of 0.1 h-1. These observations give a deep insight into the process design for a continuous succinic acid production by microorganisms.
琥珀酸通过 Actinobacillus succinogenes sp. 130Z 的连续发酵在外膜细胞循环反应器中生产,以提高活细胞浓度和生产力。使用该系统,细胞浓度在稀释率为 0.2 h-1 时增加到 16.4 g/l,比分批培养高 3 倍,琥珀酸的体积生产率在稀释率为 0.5 h-1 时增加到 6.63 g/l/h,比分批发酵高 5 倍。然而,在高稀释率下的连续培养中,观察到了一些操作问题,包括严重的膜污染和乳酸产生菌的污染。另一种琥珀酸生产者曼海姆氏菌 MBEL55E 也在该系统中得到了利用,在稀释率为 0.3 h-1 时,细胞浓度和琥珀酸的生产率分别比在稀释率为 0.1 h-1 时高 3 倍和 2.3 倍。这些观察结果深入了解了微生物连续生产琥珀酸的工艺设计。