Kim Na Yeon, Kim Sung-Koo, Ra Chae Hun
Department of Food Science and Biotechnology, College of Engineering, Global K-Food Research Center, Hankyong National University, Anseong-Si, 17579, Republic of Korea.
Department of Biotechnology, Pukyong National University, Busan, 48513, Republic of Korea.
Bioprocess Biosyst Eng. 2021 Oct;44(10):2099-2108. doi: 10.1007/s00449-021-02586-8. Epub 2021 May 25.
Lactic acid bacteria (Lactobacillus plantarum KCTC 3103) were fermented to produce gamma-aminobutyric acid (GABA). The conditions of the modified synthetic medium were optimized as 5 g/L glucose, 10 g/L yeast extract, 100 g/L rice bran extract, and 1.0 g/L ascorbic acid for GABA production. Single-step fermentation of cell growth and GABA production with a modified synthetic medium was higher than those with an MRS medium. Two-step fermentation was evaluated by separating the cell growth and GABA production under a modified synthetic medium. The cell concentration of 1.65 g dcw/L produced by the modified synthetic medium was higher than that of 1.0 g dcw/L produced by the MRS medium at 36 h from the first step of two-step fermentation. The highest GABA production of L. plantarum KCTC 3103 was 0.67 g/L with monosodium glutamate addition at 60 h in the second step of fermentation. Two-step fermentation with the modified synthetic medium is suitable for GABA production because of its high GABA productivity and favorable cell growth.
对乳酸菌(植物乳杆菌KCTC 3103)进行发酵以生产γ-氨基丁酸(GABA)。改良合成培养基的条件优化为5 g/L葡萄糖、10 g/L酵母提取物、100 g/L米糠提取物和1.0 g/L抗坏血酸用于GABA生产。使用改良合成培养基进行细胞生长和GABA生产的单步发酵高于使用MRS培养基的情况。通过在改良合成培养基下分离细胞生长和GABA生产来评估两步发酵。在两步发酵的第一步36 h时,改良合成培养基产生的细胞浓度为1.65 g干重/L,高于MRS培养基产生的1.0 g干重/L。在发酵第二步60 h添加味精时,植物乳杆菌KCTC 3103的最高GABA产量为0.67 g/L。使用改良合成培养基的两步发酵由于其高GABA生产率和良好的细胞生长而适合用于GABA生产。