Chemistry Institute, Federal University of Rio de Janeiro, Rio de Janeiro, RJ, Brazil.
School of Chemistry, Federal University of Rio de Janeiro, Rio de Janeiro, RJ, Brazil.
Braz J Microbiol. 2023 Dec;54(4):2663-2670. doi: 10.1007/s42770-023-01108-w. Epub 2023 Sep 9.
R-(+)-Perillic acid, a promising anticancer and immunomodulatory agent, is the major product from the biotransformation of R-(+)-limonene-rich orange essential oil by the yeast Yarrowia lipolytica. Due to the abundance and low cost of orange essential oil, which is a byproduct of the citrus industry, we attempted to improve the biotransformation process by optimizing yeast cell mass production. Then, the whole process was transposed and adapted to a 2-L instrumented bioreactor. Cell mass production was optimized in shaker flasks using a statistical experimental design. The optimized medium (g·L: 22.9 glucose, 7.7 peptone, 4.1 yeast extract and 1.0 malt extract) resulted in a 13.0 g·L final cell concentration and 0.18 g cell·L·h productivity. A further increase to 18.0 g·L was achieved in a 2-L bioreactor upon fed-batch culture. High-purity limonene bioconversion was performed in the same bioreactor utilizing top aeration to diminish terpene volatilization; as a result, 839.6 mg·L perillic acid accumulated after 48 h. Under the same conditions, industrial orange essential oil afforded 806.4 mg·L perillic acid. The yeast growth medium optimization resulted in a twofold increase in biomass accumulation and a reduction in growth medium nitrogen sources, which lowered the catalytic biomass production cost. Compared with conventional bottom aeration, the bioreactor top aeration strategy resulted in higher bioconversion rates. The conditions developed for high-purity limonene bioconversion were successfully applied to low-cost orange essential oil, showing the robustness of Y. lipolytica yeast.
(R-(+)- 薄荷酸是一种很有前途的抗癌和免疫调节剂,它是酵母解脂假丝酵母对富含 R-(+)-柠檬烯的橙油进行生物转化的主要产物。由于橙油是柑橘工业的副产物,其丰富且成本低廉,我们试图通过优化酵母细胞生物量生产来改进生物转化过程。然后,整个过程被移植并适应于 2-L 仪器化生物反应器。使用统计实验设计在摇瓶中优化细胞生物量生产。优化的培养基(g·L:22.9 葡萄糖、7.7 蛋白胨、4.1 酵母提取物和 1.0 麦芽提取物)最终得到 13.0 g·L 的最终细胞浓度和 0.18 g 细胞·L·h 的产率。在 2-L 生物反应器中进行分批补料培养可进一步提高到 18.0 g·L。在相同的生物反应器中利用顶部通气进行高纯度柠檬烯生物转化,以减少萜烯挥发;结果,48 h 后积累了 839.6 mg·L 的薄荷酸。在相同条件下,工业橙油提供了 806.4 mg·L 的薄荷酸。酵母生长培养基的优化导致生物量积累增加了两倍,并减少了生长培养基中的氮源,从而降低了催化生物质生产的成本。与传统的底部通气相比,生物反应器顶部通气策略导致更高的生物转化速率。成功地将高纯度柠檬烯生物转化的条件应用于低成本橙油,显示了解脂假丝酵母的稳健性。)