Department of Agricultural Biotechnology and Center for Food and Bioconvergence, Seoul National University, Seoul, 08826, Repubilc of Korea.
Department of Food Science and Technology, Chonnam National University, Gwangju, 61186, Republic of Korea.
J Biotechnol. 2019 Oct 10;304:31-37. doi: 10.1016/j.jbiotec.2019.08.009. Epub 2019 Aug 14.
2,3-Butanediol (2,3-BD) can be produced at high titers by engineered Saccharomyces cerevisiae by abolishing the ethanol biosynthetic pathway and introducing the bacterial butanediol-producing pathway. However, production of 2,3-BD instead of ethanol by engineered S. cerevisiae has resulted in glycerol production because of surplus NADH accumulation caused by a lower degree of reduction (γ = 5.5) of 2,3-BD than that (γ = 6) of ethanol. In order to eliminate glycerol production and resolve redox imbalance during 2,3-BD production, both GPD1 and GPD2 coding for glycerol-3-phosphate dehydrogenases were disrupted after overexpressing NADH oxidase from Lactococcus lactis. As disruption of the GPD genes caused growth defects due to limited supply of C compounds, Candida tropicalis PDC1 was additionally introduced to provide a necessary amount of C compounds while minimizing ethanol production. The resulting strain (BD5_T2 nox_dGPD1,2_CtPDC1) produced 99.4 g/L of 2,3-BD with 0.5 g/L glycerol accumulation in a batch culture. The fed-batch fermentation led to production of 108.6 g/L 2,3-BD with a negligible amount of glycerol production, resulting in a high BD yield (0.462 g2,3-BD/gglucose) corresponding to 92.4 % of the theoretical yield. These results demonstrate that glycerol-free production of 2,3-BD by engineered yeast is feasible.
2,3-丁二醇(2,3-BD)可以通过工程化酿酒酵母来高产量生产,方法是废除乙醇生物合成途径并引入细菌 2,3-BD 生产途径。然而,通过工程化酿酒酵母生产 2,3-BD 而不是乙醇会导致甘油生产,因为 2,3-BD 的还原程度(γ=5.5)低于乙醇(γ=6),导致 NADH 积累过剩。为了消除甘油生产并解决 2,3-BD 生产过程中的氧化还原失衡,在过表达来自乳球菌的 NADH 氧化酶后,破坏编码甘油-3-磷酸脱氢酶的 GPD1 和 GPD2。由于 GPD 基因的破坏会因 C 化合物的有限供应而导致生长缺陷,因此还引入了热带假丝酵母 PDC1,以在最小化乙醇生产的同时提供必要量的 C 化合物。所得菌株(BD5_T2nox_dGPD1,2_CtPDC1)在分批培养中生产 99.4 g/L 的 2,3-BD,同时积累 0.5 g/L 的甘油。补料分批发酵导致生产 108.6 g/L 的 2,3-BD,几乎没有甘油生产,导致高 BD 产率(0.462 g2,3-BD/gglucose),相当于理论产率的 92.4%。这些结果表明,通过工程化酵母实现无甘油的 2,3-BD 生产是可行的。