State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, 130 Meilong Road, Shanghai 200237, China.
Mar Biotechnol (NY). 2012 Dec;14(6):665-71. doi: 10.1007/s10126-012-9435-6.
An integrated control strategy of pH, shear stress, and dissolved oxygen tension (DOT) for fermentation scale-up of the marine-derived fungus Aspergillus glaucus HB 1–19 for the production of the anti-cancer compound aspergiolide A was studied. Keeping initial pH of 6.5 and shifting pH from 6.0 to 7.0 intermittently during the production phase greatly facilitated biosynthesis of aspergiolide A in shake flask cultures. Thus, a pH-shift strategy was proposed that shifting pH to 7.0 once it went lower than 6.0 by pulsed feeding NaOH solution during the production phase in bioreactor fermentation of A. glaucus HB 1–19. As a result, aspergiolide A production in a 30-L bioreactor was increased to 37.6 mg/L, which was 48.6% higher than that in 5-L bioreactor without pH shift. Fermentation scale-up was then performed in a 500-L bioreactor on the basis of an integrated criterion of near-same impeller tip velocity of early phase, DOT levels, and pH shift. The production of aspergiolide A was successfully obtained as 32.0 mg/L, which was well maintained during the process scale-up. This work offers useful information for process development of large-scale production of marine microbial metabolites.
针对海洋真菌亮灰青霉 HB 1–19 发酵生产抗癌化合物aspergiolide A,研究了一种 pH 值、剪切力和溶解氧张力(DOT)综合控制策略。在摇瓶培养中,保持初始 pH 值为 6.5 并在生产阶段间歇性地将 pH 值从 6.0 调至 7.0,这极大地促进了 aspergiolide A 的生物合成。因此,提出了一种 pH 值切换策略,即在生产阶段通过脉冲式添加 NaOH 溶液,将 pH 值从 6.0 调至 7.0,从而在亮灰青霉 HB 1–19 的生物反应器发酵中实现了 pH 值切换。结果,在 30-L 生物反应器中的 aspergiolide A 产量增加到 37.6mg/L,比没有 pH 值切换的 5-L 生物反应器中的产量提高了 48.6%。然后,根据早期阶段的近相同搅拌器尖速度、DOT 水平和 pH 值切换的综合标准,在 500-L 生物反应器中进行了发酵放大。成功获得了 32.0mg/L 的 aspergiolide A 产量,并且在过程放大过程中得到了很好的维持。这项工作为海洋微生物代谢产物的大规模生产提供了有用的信息。