Zou Jing, Chen Xiaohui, Hu Yinghong, Xiao Dongguang, Guo Xuewu, Chang Xuedong, Zhou Lisha
Chestnut Engineering Research Center of Hebei Province; Chestnut Industry Collaborative Innovation Center of Hebei Province, College of Food Science and Technology, Hebei Normal University of Science and Technology, Qinhuangdao, 066600, People's Republic of China.
Key Laboratory of Industrial Fermentation Microbiology, Ministry of Education, Tianjin Industrial Microbiology Key Laboratory; College of Biotechnology, Tianjin University of Science and Technology, Tianjin, 300457, People's Republic of China.
Biotechnol Lett. 2021 Aug;43(8):1607-1616. doi: 10.1007/s10529-021-03136-8. Epub 2021 May 2.
Development of a system for direct lactose to ethanol fermentation provides a market for the massive amounts of underutilized whey permeate made by the dairy industry. For this system, glucose and galactose metabolism were uncoupled in Saccharomyces cerevisiae by deleting two negative regulatory genes, GAL80 and MIG1, and introducing the essential lactose hydrolase LAC4 and lactose transporter LAC12, from the native but inefficient lactose fermenting yeast Kluyveromyces marxianus.
Previously, integration of the LAC4 and LAC12 genes into the MIG1 and NTH1 loci was achieved to construct strain AY-51024M. Low rates of lactose conversion led us to generate the Δmig1Δgal80 diploid mutant strain AY-GM from AY-5, which exhibited loss of diauxic growth and glucose repression, subsequently taking up galactose for consumption at a significantly higher rate and yielding higher ethanol concentrations than strain AY-51024M. Similarly, in cheese whey permeate powder solution (CWPS) during three, repeated, batch processes in a 5L bioreactor containing either 100 g/L or 150 g/L lactose, the lactose uptake and ethanol productivity rates were both significantly greater than that of AY-51024M, while the overall fermentation times were considerably lower.
Using the Cre-loxp system for deletion of the MIG1 and GAL80 genes to relieve glucose repression, and LAC4 and LAC12 overexpression to increase lactose uptake and conversion provides an efficient basis for yeast fermentation of whey permeate by-product into ethanol.
开发一种将乳糖直接发酵为乙醇的系统,可为乳制品行业产生的大量未充分利用的乳清渗透液提供市场。对于该系统,通过删除两个负调控基因GAL80和MIG1,并引入来自天然但效率低下的乳糖发酵酵母马克斯克鲁维酵母的必需乳糖水解酶LAC4和乳糖转运蛋白LAC12,使酿酒酵母中的葡萄糖和半乳糖代谢解偶联。
此前,已将LAC4和LAC12基因整合到MIG1和NTH1基因座中,构建了菌株AY-51024M。乳糖转化率低促使我们从AY-5中产生Δmig1Δgal80二倍体突变菌株AY-GM,该菌株表现出双相生长和葡萄糖阻遏的丧失,随后以明显更高的速率摄取半乳糖以供消耗,并且产生的乙醇浓度高于菌株AY-51024M。同样,在含有100 g/L或150 g/L乳糖的5L生物反应器中进行的三次重复分批过程中,在奶酪乳清渗透粉溶液(CWPS)中,乳糖摄取率和乙醇生产率均显著高于AY-51024M,而总发酵时间则显著缩短。
使用Cre-loxp系统删除MIG1和GAL80基因以解除葡萄糖阻遏,并过表达LAC4和LAC12以增加乳糖摄取和转化,为将乳清渗透液副产物酵母发酵为乙醇提供了有效的基础。