Department of Biosystems Engineering, University of Manitoba, Winnipeg, Manitoba, Canada.
Department of Genetics and Bioengineering, Izmir University of Economics, Balçova, Izmir, Turkey.
Appl Biochem Biotechnol. 2021 May;193(5):1558-1573. doi: 10.1007/s12010-021-03503-1. Epub 2021 Jan 23.
Biological hydrogen (H) is a promising candidate for production of renewable hydrogen. Using entrapped cells rather than conventional suspended cell cultures for the production of H offers several advantages, such as improved production yields related to higher cell density, and enhanced resistance to substrate and end-product inhibition. In this study, H production by a novel isolate of Clostridium intestinale (strain URNW) was evaluated using cells entrapped within 2% calcium-alginate beads under strictly anaerobic conditions. Both immobilized cells and suspended cultures were studied in sequential batch-mode anaerobic fermentation over 192 h. The production of H in the headspace was examined for four different initial cellobiose concentrations (5, 10, 20, and 40 mM). Although a lag period for initiation of the fermentation process was observed for bacteria entrapped within hydrogel beads, the immobilized cells achieved both higher volumetric production rates (mmol H/(L culture h)) and molar yields (mol H/mol glucose equivalent) of H compared with suspended cultures. In the current study, the maximum cellobiose consumption rate of 0.40 mM/h, corresponding to 133.3 mg/(L h), was achieved after 72 h of fermentation by immobilized cells, generating a high hydrogen yield of 3.57 mol H/mol cellobiose, whereas suspended cultures only yielded 1.77 mol H/mol cellobiose. The results suggest that cells remain viable within the hydrogels and proliferated with a slow rate over the course of fermentation. The stable productivity of immobilized cells over 8 days with four changes of medium depicted that the immobilized cells of the isolated strain can successfully yield higher hydrogen and lower soluble metabolites than suspended cells suggesting a feasible process for future applications for bioH production.
生物氢气(H)是生产可再生氢气的有前途的候选物。与传统的悬浮细胞培养相比,使用包埋细胞生产 H 具有许多优势,例如与更高的细胞密度相关的提高的生产产量,以及增强对基质和终产物抑制的抗性。在这项研究中,使用 2%的海藻酸钠珠内包埋的新型肠道梭菌(URNW 株)生产 H 的情况进行了评估,在严格的厌氧条件下进行。在 192 小时的顺序分批式厌氧发酵中研究了固定化细胞和悬浮培养物。对头空间中 H 的生成进行了研究,使用了四种不同的初始纤维二糖浓度(5、10、20 和 40 mM)。尽管在水凝胶珠内包埋的细菌中观察到发酵过程起始的滞后期,但与悬浮培养物相比,固定化细胞实现了更高的体积生产速率(mmol H/(L 培养物 h))和摩尔产率(mol H/mol 葡萄糖当量)的 H。在当前的研究中,固定化细胞在发酵 72 小时后达到了 0.40 mM/h 的最大纤维二糖消耗速率,对应于 133.3 mg/(L h),产生了 3.57 mol H/mol 纤维二糖的高氢气产率,而悬浮培养物仅产生 1.77 mol H/mol 纤维二糖。结果表明,细胞在水凝胶中保持活力,并在发酵过程中以缓慢的速度增殖。固定化细胞在 8 天内进行了 4 次培养基更换,具有稳定的生产力,这表明分离株的固定化细胞可以成功地产生比悬浮细胞更高的氢气和更低的可溶性代谢物,这表明该过程具有未来用于生物 H 生产的可行性。