Optimization of Fermentation Conditions for Biocatalytic Conversion of Decanoic Acid to Trans-2-Decenoic Acid

• Published in: Fermentation (Basel) 2023-12, Vol.9 (12), p.1001
• Main Authors: Nie, Shihao, Liu, Keyi, Liu, Ben, Li, Piwu, Su, Jing
• Format: Article
• Language: English
• Subjects: Acid production; Atoms & subatomic particles; Biosynthesis; Carbon; Catalysis; Chemical synthesis; Chromatography; decanoic acid; Dehydrogenases; E coli; engineered Escherichia coli; Enzymes; Fatty acids; Fermentation; Gram-positive bacteria; Industrial production; Inoculation; Inoculum; Lactose; Ligands; Liquid culture; Metabolism; Metal ions; Nanocrystals; optimization; Oxidation; response surface; trans-2-decenoic acid
• ISSN: 2311-5637; 2311-5637
• DOI: 10.3390/fermentation9121001

Trans-2-decenoic acid has a wide range of applications, including those in medicine, food, and health care. Therefore, the industrial production of trans-2-decenoic acid is particularly important. However, few studies have focused on medium-chain unsaturated fatty acids. Therefore, we aimed to optimize the fermentation process of decanoic acid biocatalysis to synthesize trans-2-decenoic acid using an engineered Escherichia coli constructed in the laboratory. Early-stage culture and the effect of the seed liquid culture time, culture temperature, inoculum amount, induction temperature, dissolution effects of the substrate solvent, metal ions, and substrate loading on the titer of trans-2-decenoic acid were evaluated. Based on a single-factor experimental optimization, a Box–Behnken design (BBD) was used for response surface testing using the substrate feeding concentration, inducer concentration, and MnCl2 concentration as response variables and trans-2-decenoic acid production as the response value. The optimal fermentation process was as follows: Seed culture time of 20 h, culture temperature of 37 °C, inoculation amount of 1%, induction temperature of 30 °C, substrate flow of 0.15 g/L, inducer concentration of 5.60 g/L, and MnCl2 concentration of 0.10 mM. Under these conditions, the average production of trans-2-decenoic acid was 1.982 ± 0.110 g/L, which was 1.042 g/L higher than that obtained in the basic LB medium. Compared with that of the previous period, the titer of the trans-2-decenoic acid studied increased by 1.501 ± 0.110 g/L, providing a basis for further research on the fermentation process of the biocatalytic decanoic acid synthesis of trans-2-decenoic acid.