Institute for Biotechnology and Bioengineering, Centre of Biological Engineering, University of Minho, 4710-057 Braga, Portugal.
Biotechnol Biofuels. 2012 Feb 13;5:6. doi: 10.1186/1754-6834-5-6.
Second generation hydrogen fermentation technologies using organic agricultural and forestry wastes are emerging. The efficient microbial fermentation of hexoses and pentoses resulting from the pretreatment of lingocellulosic materials is essential for the success of these processes.
Conversion of arabinose and glucose to hydrogen, by extreme thermophilic, anaerobic, mixed cultures was studied in continuous (70°C, pH 5.5) and batch (70°C, pH 5.5 and pH 7) assays. Two expanded granular sludge bed (EGSB) reactors, Rarab and Rgluc, were continuously fed with arabinose and glucose, respectively. No significant differences in reactor performance were observed for arabinose and glucose organic loading rates (OLR) ranging from 4.3 to 7.1 kgCOD m-3 d-1. However, for an OLR of 14.2 kgCOD m-3 d-1, hydrogen production rate and hydrogen yield were higher in Rarab than in Rgluc (average hydrogen production rate of 3.2 and 2.0 LH2 L-1 d-1 and hydrogen yield of 1.10 and 0.75 molH2 mol-1substrate for Rarab and Rgluc, respectively). Lower hydrogen production in Rgluc was associated with higher lactate production. Denaturing gradient gel electrophoresis (DGGE) results revealed no significant difference on the bacterial community composition between operational periods and between the reactors. Increased hydrogen production was observed in batch experiments when hydrogen partial pressure was kept low, both with arabinose and glucose as substrate. Sugars were completely consumed and hydrogen production stimulated (62% higher) when pH 7 was used instead of pH 5.5.
Continuous hydrogen production rate from arabinose was significantly higher than from glucose, when higher organic loading rate was used. The effect of hydrogen partial pressure on hydrogen production from glucose in batch mode was related to the extent of sugar utilization and not to the efficiency of substrate conversion to hydrogen. Furthermore, at pH 7.0, sugars uptake, hydrogen production and yield were higher than at pH 5.5, with both arabinose and glucose as substrates.
利用有机农业和林业废物的第二代氢气发酵技术正在兴起。从木质纤维素材料的预处理中获得的己糖和戊糖的高效微生物发酵对于这些过程的成功至关重要。
在连续(70°C,pH5.5)和分批(70°C,pH5.5 和 pH7)实验中,研究了极端嗜热、厌氧、混合培养物对阿拉伯糖和葡萄糖的转化为氢气。两个扩展颗粒污泥床(EGSB)反应器,Rarab 和 Rgluc,分别连续进料阿拉伯糖和葡萄糖。在阿拉伯糖和葡萄糖的有机负荷率(OLR)为 4.3 至 7.1kgCOD m-3 d-1 范围内,反应器性能没有明显差异。然而,对于 14.2kgCOD m-3 d-1 的 OLR,Rarab 中的氢气产率和氢气产率均高于 Rgluc(Rarab 和 Rgluc 的平均氢气产率分别为 3.2 和 2.0LH2 L-1 d-1,氢气产率分别为 1.10 和 0.75molH2 mol-1 底物)。Rgluc 中较低的氢气产量与较高的乳酸产量有关。变性梯度凝胶电泳(DGGE)结果表明,在运行期间和两个反应器之间,细菌群落组成没有明显差异。在批处理实验中,当保持较低的氢气分压时,观察到氢气产量增加,无论是用阿拉伯糖还是葡萄糖作为底物。当使用 pH7 代替 pH5.5 时,糖完全消耗并且氢气产量受到刺激(增加 62%)。
当使用较高的有机负荷率时,从阿拉伯糖连续生产氢气的速率明显高于从葡萄糖生产氢气的速率。在批处理模式下,氢气分压对葡萄糖产氢的影响与糖利用程度有关,而与底物转化为氢气的效率无关。此外,在 pH7.0 时,与 pH5.5 相比,以阿拉伯糖和葡萄糖为底物时,糖的摄取、氢气的产生和产率均更高。