{"title":"Enhanced fermentative γ-aminobutyric acid production by a metabolic engineered Corynebacterium glutamicum","authors":"","doi":"10.1007/s12257-024-00008-6","DOIUrl":null,"url":null,"abstract":"<h3>Abstract</h3> <p>γ-Aminobutyric acid (GABA) is a non-proteinogenic amino acid with important physiological functions, which has been widely used in food, pharmaceuticals, and polyamides production. The fermentative GABA production by <em>Corynebacterium glutamicum</em> was recognized as one of the most promising methods. However, the problems of low catalytic activity of the heterologously expressed glutamate decarboxylase (GAD) and the imbalanced carbon flux between cell growth and GABA synthesis severely limited the GABA production by <em>C. glutamicum</em>. This study applied combinational metabolic engineering and catalytic condition optimization strategies to solve these two major obstacles. The secretory expression of GAD was enhanced using a bicistronic-designed expression cassette. This bicistronic expression cassette was further triply inserted into the genome by substituting the <em>ldhA</em>, <em>pqo</em>, and <em>ack</em> genes, thus stabilizing the expression of GAD and reducing the accumulation of by-products of lactate and acetate. A growth-regulated promoter P<sub><em>CP_2836</em></sub> was applied to dynamically control the expression of <em>odhA</em>, thus controlling the α-oxoglutarate dehydrogenase complex activity for balanced cell growth and GABA production. The glutamate precursor synthesis and pyridoxal 5′-phosphate supply were also strengthened by promoter substitution. Finally, through a two-stage pH-controlled fed-batch fermentation under optimized conditions, the engineered strain reached GABA titer of 81.31 ± 1.31 g/L with a yield and productivity of 0.50 ± 0.01 g/g and 1.36 ± 0.23 g L<sup>−1</sup> h<sup>−1</sup>, which was 4.8%, 13.6%, and 11.2% higher than that of the original strain. This study laid a solid foundation for industrial fermentative GABA production by engineered <em>C. glutamicum</em>.</p>","PeriodicalId":8936,"journal":{"name":"Biotechnology and Bioprocess Engineering","volume":"168-169 1","pages":""},"PeriodicalIF":2.5000,"publicationDate":"2024-02-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Biotechnology and Bioprocess Engineering","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1007/s12257-024-00008-6","RegionNum":4,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"BIOTECHNOLOGY & APPLIED MICROBIOLOGY","Score":null,"Total":0}
引用次数: 0
Abstract
γ-Aminobutyric acid (GABA) is a non-proteinogenic amino acid with important physiological functions, which has been widely used in food, pharmaceuticals, and polyamides production. The fermentative GABA production by Corynebacterium glutamicum was recognized as one of the most promising methods. However, the problems of low catalytic activity of the heterologously expressed glutamate decarboxylase (GAD) and the imbalanced carbon flux between cell growth and GABA synthesis severely limited the GABA production by C. glutamicum. This study applied combinational metabolic engineering and catalytic condition optimization strategies to solve these two major obstacles. The secretory expression of GAD was enhanced using a bicistronic-designed expression cassette. This bicistronic expression cassette was further triply inserted into the genome by substituting the ldhA, pqo, and ack genes, thus stabilizing the expression of GAD and reducing the accumulation of by-products of lactate and acetate. A growth-regulated promoter PCP_2836 was applied to dynamically control the expression of odhA, thus controlling the α-oxoglutarate dehydrogenase complex activity for balanced cell growth and GABA production. The glutamate precursor synthesis and pyridoxal 5′-phosphate supply were also strengthened by promoter substitution. Finally, through a two-stage pH-controlled fed-batch fermentation under optimized conditions, the engineered strain reached GABA titer of 81.31 ± 1.31 g/L with a yield and productivity of 0.50 ± 0.01 g/g and 1.36 ± 0.23 g L−1 h−1, which was 4.8%, 13.6%, and 11.2% higher than that of the original strain. This study laid a solid foundation for industrial fermentative GABA production by engineered C. glutamicum.
期刊介绍：
Biotechnology and Bioprocess Engineering is an international bimonthly journal published by the Korean Society for Biotechnology and Bioengineering. BBE is devoted to the advancement in science and technology in the wide area of biotechnology, bioengineering, and (bio)medical engineering. This includes but is not limited to applied molecular and cell biology, engineered biocatalysis and biotransformation, metabolic engineering and systems biology, bioseparation and bioprocess engineering, cell culture technology, environmental and food biotechnology, pharmaceutics and biopharmaceutics, biomaterials engineering, nanobiotechnology, and biosensor and bioelectronics.
求助内容：
应助结果提醒方式：
京公网安备 11010802042870号
