| Autor: |
Zhang L; Zhejiang Engineering Research Center of Industrial Biocatalysis and Transformation, Changxing Pharmaceutical Co. Ltd., Changxing 313100, Zhejiang, China., Xiao Y; Zhejiang Engineering Research Center of Industrial Biocatalysis and Transformation, Changxing Pharmaceutical Co. Ltd., Changxing 313100, Zhejiang, China., Yang W; Zhejiang Engineering Research Center of Industrial Biocatalysis and Transformation, Changxing Pharmaceutical Co. Ltd., Changxing 313100, Zhejiang, China., Hua C; Zhejiang Engineering Research Center of Industrial Biocatalysis and Transformation, Changxing Pharmaceutical Co. Ltd., Changxing 313100, Zhejiang, China., Wang Y; Zhejiang Engineering Research Center of Industrial Biocatalysis and Transformation, Changxing Pharmaceutical Co. Ltd., Changxing 313100, Zhejiang, China., Li J; Zhejiang Engineering Research Center of Industrial Biocatalysis and Transformation, Changxing Pharmaceutical Co. Ltd., Changxing 313100, Zhejiang, China., Yang T; School of Biotechnology, Jiangnan University, Wuxi 214122, Jiangsu, China. |
| Abstrakt: |
In this study, Escherichia coli BL21 (DE3) was used as the host to construct 2 recombinant E. coli strains that co-expressed leucine dehydrogenase (LDH, Bacillus cereus)/formate dehydrogenase (FDH, Ancylobacter aquaticus), or leucine dehydrogenase (LDH, Bacillus cereus)/alcohol dehydrogenase (ADH, Rhodococcus), respectively. L-2-aminobutyric acid was then synthesized by L-threonine deaminase (L-TD) with LDH-FDH or LDH-ADH by coupling with two different NADH regeneration systems. LDH-FDH process and LDH-ADH process were optimized and compared with each other. The optimum reaction pH of LDH-FDH process was 7.5, and the optimum reaction temperature was 35 °C. After 28 h, the concentration of L-2-aminobutyric acid was 161.8 g/L with a yield of 97%, when adding L-threonine in batches for controlling 2-ketobutyric acid concentration less than 15 g/L and using 50 g/L ammonium formate, 0.3 g/L NAD+, 10% LDH-FDH crude enzyme solution (V/V) and 7 500 U/L L-TD. The optimum reaction pH of LDH-ADH process was 8.0, and the optimum reaction temperature was 35 °C. After 24 h, the concentration of L-2-aminobutyric acid was 119.6 g/L with a yield of 98%, when adding L-threonine and isopropanol (1.2 times of L-threonine) in batches for controlling 2-ketobutyric acid concentration less than 15 g/L, removing acetone in time and using 0.3 g/L NAD⁺, 10% LDH-ADH crude enzyme solution (V/V) and 7 500 U/L L-TD. The process and results used in this paper provide a reference for the industrialization of L-2-aminobutyric acid. |
