{"title":"调整大肠杆菌 W3110 的主要生物合成模块以提高 l-高丝氨酸的产量","authors":"Kun Niu, Rui Zheng, Miao Zhang, Mao‐Qin Chen, Yi‐Ming Kong, Zhi‐Qiang Liu, Yu‐Guo Zheng","doi":"10.1002/bit.28861","DOIUrl":null,"url":null,"abstract":"<jats:sc>l</jats:sc>‐homoserine is an important platform compound of many valuable products. Construction of microbial cell factory for <jats:sc>l</jats:sc>‐homoserine production from glucose has attracted a great deal of attention. In this study, <jats:sc>l</jats:sc>‐homoserine biosynthesis pathway was divided into three modules, the glucose uptake and upstream pathway, the downstream pathway, and the energy supply module. Metabolomics of the chassis strain HS indicated that the supply of ATP was inadequate, therefore, the energy supply module was firstly modified. By balancing the ATP supply module, the <jats:sc>l</jats:sc>‐homoserine production increased by 66% to 12.55 g/L. Further, the results indicated that the upstream pathway was blocked, and increasing the culture temperature to 37°C could solve this problem and the <jats:sc>l</jats:sc>‐homoserine production reached 21.38 g/L. Then, the downstream synthesis pathways were further strengthened to balance the fluxes, and the <jats:sc>l</jats:sc>‐homoserine production reached the highest reported level of 32.55 g/L in shake flasks. Finally, fed‐batch fermentation in a 5‐L bioreactor was conducted, and <jats:sc>l</jats:sc>‐homoserine production could reach to 119.96 g/L after 92 h cultivation, with the yield of 0.41 g/g glucose and productivity of 1.31 g/L/h. The study provides a well research foundation for <jats:sc>l</jats:sc>‐homoserine production by microbial fermentation with the capacity for industrial application.","PeriodicalId":9168,"journal":{"name":"Biotechnology and Bioengineering","volume":"14 1","pages":""},"PeriodicalIF":3.5000,"publicationDate":"2024-10-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Adjustment of the main biosynthesis modules to enhance the production of l‐homoserine in Escherichia coli W3110\",\"authors\":\"Kun Niu, Rui Zheng, Miao Zhang, Mao‐Qin Chen, Yi‐Ming Kong, Zhi‐Qiang Liu, Yu‐Guo Zheng\",\"doi\":\"10.1002/bit.28861\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<jats:sc>l</jats:sc>‐homoserine is an important platform compound of many valuable products. Construction of microbial cell factory for <jats:sc>l</jats:sc>‐homoserine production from glucose has attracted a great deal of attention. In this study, <jats:sc>l</jats:sc>‐homoserine biosynthesis pathway was divided into three modules, the glucose uptake and upstream pathway, the downstream pathway, and the energy supply module. Metabolomics of the chassis strain HS indicated that the supply of ATP was inadequate, therefore, the energy supply module was firstly modified. By balancing the ATP supply module, the <jats:sc>l</jats:sc>‐homoserine production increased by 66% to 12.55 g/L. Further, the results indicated that the upstream pathway was blocked, and increasing the culture temperature to 37°C could solve this problem and the <jats:sc>l</jats:sc>‐homoserine production reached 21.38 g/L. Then, the downstream synthesis pathways were further strengthened to balance the fluxes, and the <jats:sc>l</jats:sc>‐homoserine production reached the highest reported level of 32.55 g/L in shake flasks. Finally, fed‐batch fermentation in a 5‐L bioreactor was conducted, and <jats:sc>l</jats:sc>‐homoserine production could reach to 119.96 g/L after 92 h cultivation, with the yield of 0.41 g/g glucose and productivity of 1.31 g/L/h. The study provides a well research foundation for <jats:sc>l</jats:sc>‐homoserine production by microbial fermentation with the capacity for industrial application.\",\"PeriodicalId\":9168,\"journal\":{\"name\":\"Biotechnology and Bioengineering\",\"volume\":\"14 1\",\"pages\":\"\"},\"PeriodicalIF\":3.5000,\"publicationDate\":\"2024-10-19\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Biotechnology and Bioengineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://doi.org/10.1002/bit.28861\",\"RegionNum\":2,\"RegionCategory\":\"生物学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"BIOTECHNOLOGY & APPLIED MICROBIOLOGY\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Biotechnology and Bioengineering","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1002/bit.28861","RegionNum":2,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"BIOTECHNOLOGY & APPLIED MICROBIOLOGY","Score":null,"Total":0}
引用次数: 0
摘要
l-高丝氨酸是许多有价值产品的重要平台化合物。构建以葡萄糖为原料生产 l-高丝氨酸的微生物细胞工厂引起了广泛关注。本研究将 l-高丝氨酸的生物合成途径分为三个模块,即葡萄糖摄取及上游途径、下游途径和能量供应模块。基质菌株 HS 的代谢组学研究表明 ATP 供应不足,因此首先对能量供应模块进行了改造。通过平衡 ATP 供应模块,l-高丝氨酸的产量增加了 66%,达到 12.55 克/升。此外,结果表明上游途径受阻,将培养温度提高到 37°C 可以解决这一问题,l-高丝氨酸产量达到 21.38 克/升。然后,进一步加强下游合成途径以平衡通量,在摇瓶中,l-高丝氨酸的产量达到了所报道的最高水平,即 32.55 克/升。最后,在 5 升生物反应器中进行饲料批量发酵,经过 92 h 的培养,l-高丝氨酸产量达到 119.96 g/L,葡萄糖产量为 0.41 g/g,生产率为 1.31 g/L/h。该研究为微生物发酵法生产 l-高丝氨酸提供了良好的研究基础,并具有工业应用能力。
Adjustment of the main biosynthesis modules to enhance the production of l‐homoserine in Escherichia coli W3110
l‐homoserine is an important platform compound of many valuable products. Construction of microbial cell factory for l‐homoserine production from glucose has attracted a great deal of attention. In this study, l‐homoserine biosynthesis pathway was divided into three modules, the glucose uptake and upstream pathway, the downstream pathway, and the energy supply module. Metabolomics of the chassis strain HS indicated that the supply of ATP was inadequate, therefore, the energy supply module was firstly modified. By balancing the ATP supply module, the l‐homoserine production increased by 66% to 12.55 g/L. Further, the results indicated that the upstream pathway was blocked, and increasing the culture temperature to 37°C could solve this problem and the l‐homoserine production reached 21.38 g/L. Then, the downstream synthesis pathways were further strengthened to balance the fluxes, and the l‐homoserine production reached the highest reported level of 32.55 g/L in shake flasks. Finally, fed‐batch fermentation in a 5‐L bioreactor was conducted, and l‐homoserine production could reach to 119.96 g/L after 92 h cultivation, with the yield of 0.41 g/g glucose and productivity of 1.31 g/L/h. The study provides a well research foundation for l‐homoserine production by microbial fermentation with the capacity for industrial application.
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