Mol Michael, Ardila Magda Stephania, Mol Bronwyn Ashleigh, Aliyu Habibu, Neumann Anke, de Maayer Pieter
School of Molecular and Cell Biology, Faculty of Science, University of the Witwatersrand, Johannesburg, 2000, South Africa.
Section II: Electrobiotechnology, Institute of Process Engineering in Life Science, Karlsruhe Institute of Technology, 76131, Karlsruhe, Germany.
Microb Cell Fact. 2024 May 2;23(1):125. doi: 10.1186/s12934-024-02391-4.
The facultatively anaerobic thermophile Parageobacillus thermoglucosidasius is able to produce hydrogen gas (H) through the water-gas shift (WGS) reaction. To date this process has been evaluated under controlled conditions, with gas feedstocks comprising carbon monoxide and variable proportions of air, nitrogen and hydrogen. Ultimately, an economically viable hydrogenogenic system would make use of industrial waste/synthesis gases that contain high levels of carbon monoxide, but which may also contain contaminants such as H, oxygen (O) and other impurities, which may be toxic to P. thermoglucosidasius.
We evaluated the effects of synthesis gas (syngas) mimetic feedstocks on WGS reaction-driven H gas production by P. thermoglucosidasius DSM 6285 in small-scale fermentations. Improved H gas production yields and faster onset towards hydrogen production were observed when anaerobic synthetic syngas feedstocks were used, at the expense of biomass accumulation. Furthermore, as the WGS reaction is an anoxygenic process, we evaluated the influence of O perturbation on P. thermoglucosidasius hydrogenogenesis. O supplementation improved biomass accumulation, but reduced hydrogen yields in accordance with the level of oxygen supplied. However, H gas production was observed at low O levels. Supplementation also induced rapid acetate consumption, likely to sustain growth.
The utilisation of anaerobic syngas mimetic gas feedstocks to produce H and the relative flexibility of the P. thermoglucosidasius WGS reaction system following O perturbation further supports its applicability towards more robust and continuous hydrogenogenic operation.
兼性厌氧嗜热菌嗜热葡糖苷芽孢杆菌能够通过水煤气变换(WGS)反应产生氢气(H₂)。迄今为止,该过程已在受控条件下进行评估,气体原料包括一氧化碳以及不同比例的空气、氮气和氢气。最终,一个经济可行的产氢系统将利用含有高浓度一氧化碳但也可能含有诸如H₂、氧气(O₂)和其他杂质等污染物的工业废料/合成气,这些污染物可能对嗜热葡糖苷芽孢杆菌有毒。
我们在小规模发酵中评估了合成气模拟原料对嗜热葡糖苷芽孢杆菌DSM 6285的WGS反应驱动的H₂气体产生的影响。当使用厌氧合成气原料时,观察到H₂气体产率提高且产氢起始更快,但以生物量积累为代价。此外,由于WGS反应是一个不产氧的过程,我们评估了O₂扰动对嗜热葡糖苷芽孢杆菌产氢的影响。补充O₂改善了生物量积累,但根据供应的氧气水平降低了氢气产率。然而,在低O₂水平下观察到了H₂气体产生。补充O₂还诱导了乙酸盐的快速消耗,这可能维持生长。
利用厌氧合成气模拟气体原料生产H₂以及嗜热葡糖苷芽孢杆菌WGS反应系统在O₂扰动后的相对灵活性,进一步支持了其在更稳健和连续的产氢操作中的适用性。