State Key Laboratory of Food Science and Technology, Jiangnan University, Wuxi, Jiangsu 214122, China.
International Joint Laboratory on Food Safety, Jiangnan University, Wuxi 214122, China.
J Agric Food Chem. 2021 Mar 31;69(12):3702-3711. doi: 10.1021/acs.jafc.1c00246. Epub 2021 Mar 23.
Lacto--triose II (LNT II), a core structural unit of human milk oligosaccharides (HMOs), has attracted substantial attention for its nutraceutical potentials and applications in the production of complex HMOs. In this study, was metabolically engineered to efficiently produce LNT II using glycerol as a carbon source and lactose as a substrate. The UDP--acetylglucosamine (UDP-GlcNAc) biosynthesis pathway was strengthened, and β-1,3--acetylglucosaminyltransferase (LgtA) was introduced to construct an LNT II-producing base strain. To increase the titer and yield of LNT II, combinatorial optimization of the copy number and the ribosomal binding site sequence was performed to tune the gene expression strength and translation rates of the pathway enzymes. Next, multipoint mutations were introduced to glucosamine-6-phosphatesynthase (GlmS) to relieve the feedback inhibition. Then, a series of engineered strains were constructed by blocking the futile pathways by the deletion of the relevant genes. Finally, the culture conditions were optimized. LNT II titer was improved step-by-step from 0.53 to 5.52 g/L in shake-flask cultivations. Fed-batch culture of the final engineered strain produced 46.2 g/L of LNT II, with an LNT II productivity and content of 0.77 g/(L·h) and 0.95 g/g dry cell weight, respectively.
乳糖三糖 II(LNT II)是母乳低聚糖(HMOs)的核心结构单元,由于其具有营养保健品的潜力,并可应用于复杂 HMOs 的生产,因此引起了广泛关注。在本研究中,利用甘油作为碳源和乳糖作为底物,通过代谢工程对 进行了改造,以高效生产 LNT II。强化了 UDP-乙酰葡萄糖胺(UDP-GlcNAc)生物合成途径,并引入了β-1,3-乙酰氨基葡萄糖基转移酶(LgtA),构建了 LNT II 生产的基础菌株。为了提高 LNT II 的产量和得率,对途径酶的拷贝数和核糖体结合位点序列进行了组合优化,以调节基因表达强度和翻译效率。接下来,对葡萄糖胺-6-磷酸合酶(GlmS)进行多点突变,以缓解反馈抑制。然后,通过删除相关基因来阻断无效途径,构建了一系列工程菌株。最后,对培养条件进行了优化。在摇瓶培养中,LNT II 的产量逐步从 0.53 g/L 提高到 5.52 g/L。最后工程菌株的分批补料培养生产了 46.2 g/L 的 LNT II,LNT II 的生产速率和含量分别为 0.77 g/(L·h)和 0.95 g/g 干细胞重量。