Ardila Magda S, Aliyu Habibu, de Maayer Pieter, Neumann Anke
Section II: Electrobiotechnology, Institute of Process Engineering in Life Science, Karlsruhe Institute of Technology, 76131, Karlsruhe, Germany.
Section V: Biotechnology and Microbial Genetics, Institute for Biological Interfaces, Karlsruhe Institute of Technology, 76131, Karlsruhe, Germany.
Biotechnol Biofuels Bioprod. 2025 Jan 9;18(1):3. doi: 10.1186/s13068-024-02597-z.
Parageobacillus thermoglucosidasius is a facultatively anaerobic thermophile that is able to produce hydrogen (H) gas from the oxidation of carbon monoxide through the water-gas shift reaction when grown under anaerobic conditions. The water-gas shift (WGS) reaction is driven by a carbon monoxide dehydrogenase-hydrogenase enzyme complex. Previous experiments exploring hydrogenogenesis with P. thermoglucosidasius have relied on batch fermentations comprising defined media compositions and gas atmospheres. This study evaluated the effects of a semi-continuous feeding strategy on hydrogenogenesis.
A batch and two semi-continuous fermentations, with feeding of the latter fresh media (with glucose) in either 24 h or 48 h intervals were undertaken and H production, carbon monoxide dehydrogenase (CODH) activity, and metabolite consumption/production were monitored throughout. Maximum H production rates (HPR) of 0.14 and 0.3 mmol min, were observed for the batch and the semi-continuous fermentations, respectively. Daily feeding attained stable H production for 7 days, while feeding every 48 h resulted in high variations in H production. CODH enzyme activity correlated with H production, with a maximum of 1651 U mL on day 14 with the 48 h feeding strategy, while CODH activity remained relatively constant throughout the fermentation process with the 24 h feeding strategy.
The results emphasize the significance of a semi-continuous glucose-containing feed for attaining stable hydrogen production with P. thermoglucosidasius. The semi-continuous fermentations achieved a 46% higher HPR than the batch fermentation. The higher HPRs achieved with both semi-continuous fermentations imply that this approach could enhance the biohydrogen platform. However, optimizing the feeding interval is pivotal to ensuring stable hydrogen production.
嗜热栖热放线菌是一种兼性厌氧嗜热菌,在厌氧条件下生长时,能够通过水煤气变换反应将一氧化碳氧化产生氢气(H₂)。水煤气变换(WGS)反应由一氧化碳脱氢酶 - 氢化酶酶复合物驱动。以往关于嗜热栖热放线菌产氢的实验依赖于包含特定培养基成分和气体氛围的分批发酵。本研究评估了半连续补料策略对产氢的影响。
进行了一次分批发酵和两次半连续发酵,后者分别以24小时或48小时的间隔补加新鲜培养基(含葡萄糖),并全程监测氢气产量、一氧化碳脱氢酶(CODH)活性以及代谢产物的消耗/生成情况。分批发酵和半连续发酵的最大氢气产率(HPR)分别为0.14和0.3 mmol/min。每日补料可使氢气产量稳定7天,而每48小时补料一次则导致氢气产量波动较大。CODH酶活性与氢气产量相关,采用48小时补料策略时,第14天的CODH活性最高,为1651 U/mL,而采用24小时补料策略时,CODH活性在整个发酵过程中保持相对稳定。
结果强调了半连续含葡萄糖补料对于嗜热栖热放线菌实现稳定产氢的重要性。半连续发酵的HPR比分批发酵高46%。两种半连续发酵均实现了更高的HPR,这意味着该方法可以增强生物制氢平台。然而,优化补料间隔对于确保稳定产氢至关重要。