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利用源自核梭杆菌的酪氨酸酚裂解酶的重组大肠杆菌高效生物合成 L-DOPA 的工艺开发。

Process development for efficient biosynthesis of L-DOPA with recombinant Escherichia coli harboring tyrosine phenol lyase from Fusobacterium nucleatum.

机构信息

Key Laboratory of Bioorganic Synthesis of Zhejiang Province, College of Biotechnology and Bioengineering, Zhejiang University of Technology, Hangzhou, 310014, People's Republic of China.

Engineering Research Center of Bioconversion and Biopurification of Ministry of Education, Zhejiang University of Technology, Hangzhou, 310014, People's Republic of China.

出版信息

Bioprocess Biosyst Eng. 2018 Sep;41(9):1347-1354. doi: 10.1007/s00449-018-1962-8. Epub 2018 Jun 5.

Abstract

The tyrosine phenol lyase (TPL) catalyzed synthesis of L-DOPA was regarded as one of the most economic route for L-DOPA synthesis. In our previous study, a novel TPL from Fusobacterium nucleatum (Fn-TPL) was exploited for efficient biosynthesis of L-DOPA. However, the catalytic efficiency decreased when the reaction system expanded from 100 mL to 1 L. As such, the bioprocess for scale-up production of L-DOPA was developed in this study. To increase the stability of substrate and product, as well as decrease the by-product formation, the optimum temperature and pH were determined to be 15 °C and pH 8.0, respectively. The initial concentration of pyrocatechol, pyruvate and ammonium acetate was fixed at 8, 5 and 77 g/L and a fed-batch approach was applied with sodium pyruvate, pyrocatechol and ammonium acetate fed in a concentration of 5, 5 and 3.5 g/L, respectively. In addition, L-DOPA crystals were exogenously added to inhibit cell encapsulation by the precipitated product. The final L-DOPA concentration reached higher than 120 g/L with pyrocatechol conversion more than 96% in a 15-L stirred tank, demonstrating the great potential of Fn-TPL for industrial production of L-DOPA.

摘要

酪氨酸苯酚裂解酶(TPL)催化的 L-DOPA 合成被认为是 L-DOPA 合成最经济的途径之一。在我们之前的研究中,利用来自核梭杆菌(Fn-TPL)的新型 TPL 进行了高效的 L-DOPA 生物合成。然而,当反应体系从 100mL 扩大到 1L 时,催化效率降低。因此,本研究开发了 L-DOPA 规模化生产的生物工艺。为了提高底物和产物的稳定性,减少副产物的形成,确定了最佳温度和 pH 值分别为 15°C 和 pH 8.0。焦儿茶酚、丙酮酸和乙酸铵的初始浓度分别固定在 8、5 和 77g/L,并采用分批补料的方法,分别以 5、5 和 3.5g/L 的浓度补加丙酮酸、焦儿茶酚和乙酸铵。此外,还添加了 L-DOPA 晶体以抑制沉淀产物对细胞的包埋。在 15L 搅拌罐中,最终 L-DOPA 浓度达到 120g/L 以上,焦儿茶酚转化率超过 96%,表明 Fn-TPL 具有用于 L-DOPA 工业化生产的巨大潜力。

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