Key Laboratory of Carbohydrate Chemistry and Biotechnology, Ministry of Education, School of Biotechnology, Jiangnan University, Wuxi, 214122, China.
Department of Chemical and Biomolecular Engineering, The Ohio State University, Columbus, OH, 43210, USA.
Bioprocess Biosyst Eng. 2020 Aug;43(8):1479-1486. doi: 10.1007/s00449-020-02341-5. Epub 2020 Apr 11.
Endo-β-1,3-glucanase is used to hydrolyze curdlan in a wide range of oligosaccharides production processes. Using pachymaran as the sole carbon source resulted in an endo-β-1,3-glucanase activity of 86.1 U/mL and an E/E ratio of 0.43, which were 3.2 and 1.65 folds of the values from control (glucose as the sole carbon source), due to the inductive effect of pachymaran as a polysaccharide. However, the cell concentration decreased from 25 to 12 g/L during the late fermentation phase. Therefore, a novel multi-stage feeding strategy was developed wherein glucose was fed twice during the cell logarithmic growth phase (24 and 48 h) and pachymaran once during the early stage of the enzyme accumulation phase (72 h). Consequently, the cell concentration remained around 30 g/L during the late fermentation phase. Endo-β-1,3-glucanase activity and E/E reached 160.0 U/mL and 0.76, respectively, which were 6.0 and 2.92 folds of the values from control. In addition, three typical polysaccharides with β-1,3-linked glucose residues were successfully hydrolyzed by endo-β-1,3-glucanase to produce multifunctional β-1,3-oligoglucosides.
内切-β-1,3-葡聚糖酶被广泛用于水解多种寡糖生产工艺中的支链淀粉。以几丁质为唯一碳源时,内切-β-1,3-葡聚糖酶的酶活为 86.1 U/mL,E/E 值为 0.43,分别是葡萄糖为唯一碳源时的 3.2 倍和 1.65 倍,这是由于几丁质作为多糖的诱导作用。然而,在发酵后期,细胞浓度从 25 g/L 下降到 12 g/L。因此,开发了一种新型多阶段补料策略,即在细胞对数生长期(24 和 48 h)补加两次葡萄糖,在酶积累早期(72 h)补加一次几丁质。结果,发酵后期细胞浓度保持在 30 g/L 左右。内切-β-1,3-葡聚糖酶的酶活和 E/E 分别达到 160.0 U/mL 和 0.76,分别是对照的 6.0 倍和 2.92 倍。此外,三种典型的具有β-1,3 连接葡萄糖残基的多糖被内切-β-1,3-葡聚糖酶成功水解,生成多功能β-1,3-寡葡糖苷。