Laura Keitel, Katharina Miebach, Lea Rummel, Stanislav Yordanov, Jochen Büchs
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In this work, axenic cultures were studied in a shake flask and 2 L fermenter scale to characterize the influence of initial pH, buffer concentration, osmolality, and product inhibition on growth and organic acid production by P. vulgatus. Both cultivation systems had online gas measurements for total gas and CO2 production. HPLC analysis generated closed carbon balances, accounting for all produced acids. Total gas transfer rates and CO2 transfer rates revealed that 65% of produced gas was attributed to H2, while just 35% was connected to CO2 production. A minimum buffer concentration of 50 mM MOPS and an initial pH of 7.3 were identified to mitigate pH inhibition in P. vulgatus cultivations with a defined minimal medium and glucose as substrate. The initial addition of lactate showed an inhibitory effect, starting at a concentration of 1 g L−1. On the contrary, initial acetate addition was beneficial for organic acid production. A comparison of a pH-buffered and a pH-controlled 2 L fermentation demonstrated a switch in acid production toward succinate under pH control. The study provides insight into improved cultivation conditions for the gut bacterium P. vulgatus and demonstrates a successful scale-up from the shake flask to the 2 L bioreactor. By applying pH control in the bioreactor, growth was increased, and the organic acid production was switched from lactate to succinate. 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A minimum buffer concentration of 50 mM MOPS and an initial pH of 7.3 were identified to mitigate pH inhibition in P. vulgatus cultivations with a defined minimal medium and glucose as substrate. The initial addition of lactate showed an inhibitory effect, starting at a concentration of 1 g L−1. On the contrary, initial acetate addition was beneficial for organic acid production. A comparison of a pH-buffered and a pH-controlled 2 L fermentation demonstrated a switch in acid production toward succinate under pH control. The study provides insight into improved cultivation conditions for the gut bacterium P. vulgatus and demonstrates a successful scale-up from the shake flask to the 2 L bioreactor. By applying pH control in the bioreactor, growth was increased, and the organic acid production was switched from lactate to succinate. 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引用次数: 0
摘要
厌氧肠道细菌 Phocaeicola vulgatus(原名 Bacteroides vulgatus)在人类肠道微生物组中发挥着重要作用。它可以产生具有抗菌特性的生物活性化合物以及琥珀酸等与工业相关的有机酸。然而,由于肠道厌氧菌的培养具有挑战性,而且通常是在富集微生物群培养物的情况下进行的,因此在了解 P. vulgatus 的新陈代谢方面还存在知识空白。我们的目标是通过在不同的培养条件和规模下描述这种厌氧菌的特征来填补这一空白。在这项工作中,我们研究了摇瓶和 2 升发酵罐中的轴生培养物,以确定初始 pH 值、缓冲液浓度、渗透压和产物抑制对 P. vulgatus 的生长和有机酸生产的影响。两种培养系统都有在线气体测量功能,用于测量总气体和二氧化碳的产生量。高效液相色谱分析得出了封闭的碳平衡,计算了所有产生的酸。总气体转移率和二氧化碳转移率显示,产生的气体中有 65% 是 H2,只有 35% 与二氧化碳的产生有关。确定了 50 mM MOPS 的最低缓冲浓度和 7.3 的初始 pH 值,以减轻以葡萄糖为底物的最低培养基对 P. vulgatus 的 pH 抑制作用。乳酸盐的初始添加浓度为 1 g L-1 时,会产生抑制作用。相反,初始添加醋酸盐有利于有机酸的产生。对 pH 缓冲发酵和 pH 受控的 2 升发酵进行比较后发现,在 pH 受控的情况下,酸的生产转向琥珀酸。这项研究深入探讨了肠道细菌 P. vulgatus 的改进培养条件,并证明了从摇瓶到 2 升生物反应器的成功放大。通过在生物反应器中应用 pH 控制,生长得到了提高,有机酸的生产也从乳酸转为琥珀酸。尽管 P. vulgatus 可以作为一种生产有趣的生物活性化合物和有机酸的生物体,但要提高滴度,还需要进一步的表征和改进。
Process analysis of the anaerobe Phocaeicola vulgatus in a shake flasks and fermenter reveals pH and product inhibition
The anaerobic gut bacterium Phocaeicola vulgatus (formerly Bacteroides vulgatus) has a significant role in the human gut microbiome. It can produce bioactive compounds with antimicrobial properties and industrially relevant organic acids like succinate. However, there is a knowledge gap in understanding the metabolism of P. vulgatus, as cultivation of anaerobic gut bacteria is challenging and usually conducted with enriched microbiota cultures. We aim to close this gap by characterizing this anaerobe bacterium in different cultivation conditions and scales. In this work, axenic cultures were studied in a shake flask and 2 L fermenter scale to characterize the influence of initial pH, buffer concentration, osmolality, and product inhibition on growth and organic acid production by P. vulgatus. Both cultivation systems had online gas measurements for total gas and CO2 production. HPLC analysis generated closed carbon balances, accounting for all produced acids. Total gas transfer rates and CO2 transfer rates revealed that 65% of produced gas was attributed to H2, while just 35% was connected to CO2 production. A minimum buffer concentration of 50 mM MOPS and an initial pH of 7.3 were identified to mitigate pH inhibition in P. vulgatus cultivations with a defined minimal medium and glucose as substrate. The initial addition of lactate showed an inhibitory effect, starting at a concentration of 1 g L−1. On the contrary, initial acetate addition was beneficial for organic acid production. A comparison of a pH-buffered and a pH-controlled 2 L fermentation demonstrated a switch in acid production toward succinate under pH control. The study provides insight into improved cultivation conditions for the gut bacterium P. vulgatus and demonstrates a successful scale-up from the shake flask to the 2 L bioreactor. By applying pH control in the bioreactor, growth was increased, and the organic acid production was switched from lactate to succinate. Even though P. vulgatus could serve as a production organism for interesting bioactive compounds and organic acids, further characterization and improvement are necessary to improve titers.