Sun Lihui, Yu Feifei, Zheng Yuguo
Institute of Bioengineering, Zhejiang University of Technology, Hangzhou 310032, Zhejiang, China.
Sheng Wu Gong Cheng Xue Bao. 2012 Apr;28(4):498-507.
3-Hydroxypropionic acid is an important building block to synthesize lots of industrially valuable chemicals. In this study, we firstly investigated the effects of cell, substrate and product concentrations on biosynthesis of 3-hydroxypropionic acid from 1,3-propanediol by Gluconobacter oxydans ZJB09112 in 50-mL shake flask containing 10 mL transformation liquid. To avoid the inhibition of substrate and product, we adopted fed-batch biotransformation and fed-batch biotransformation coupled with in situ product removal in 2-L bubble column reactor containing 1 L transformation liquid. The results show that high concentrations of substrate and product could inhibit the biotransformation by decreasing the initial reaction rate, and the optimal reaction conditions were as follows: cell concentration 6 g/L, pH 5.5. Fed-batch biotransformation in which the substrate concentration was maintained at 15-20 g/L could obtain product concentration of 60.8 g/L after 60 h, which gave a productivity of 1.0 g/(Lh) and a yield of 84.3%. Furthermore, fed-batch biotransformation coupled with in situ product removal could achieve the total product concentration of 76.3 g/L after 50 h, which gave a productivity of 1.5 g/(L x h) and a yield of 83.7%. The results obtained here may be useful for the application of G. oxydans in biocatalysis industry by using its characteristic of incomplete oxidation of alcohols.
3-羟基丙酸是合成许多具有工业价值化学品的重要原料。在本研究中,我们首先在装有10 mL转化液的50 mL摇瓶中,研究了细胞、底物和产物浓度对氧化葡萄糖酸杆菌ZJB09112由1,3-丙二醇生物合成3-羟基丙酸的影响。为避免底物和产物的抑制作用,我们在装有1 L转化液的2 L鼓泡塔反应器中采用分批补料生物转化以及分批补料生物转化与产物原位去除相结合的方法。结果表明,高浓度的底物和产物会通过降低初始反应速率来抑制生物转化,最佳反应条件如下:细胞浓度6 g/L,pH 5.5。在分批补料生物转化中,将底物浓度维持在15 - 20 g/L,60 h后可获得产物浓度60.8 g/L,生产效率为1.0 g/(L·h),产率为84.3%。此外,分批补料生物转化与产物原位去除相结合,50 h后可实现总产物浓度76.3 g/L,生产效率为1.5 g/(L·h),产率为83.7%。通过利用氧化葡萄糖酸杆菌不完全氧化醇类的特性,本研究结果可能有助于其在生物催化工业中的应用。