Chin Hsien-Long, Chen Zu-Shia, Chou C Perry
Department of Chemical Engineering, Feng Chia University, Taichung, Taiwan 407, ROC.
Biotechnol Prog. 2003 Mar-Apr;19(2):383-8. doi: 10.1021/bp0200604.
We demonstrated the feasibility of fedbatch operation using Clostridium acetobutylicum suspension culture as a biocatalyst for the continuous production of hydrogen. The optimum operating pH and temperature of the current cultivation system for hydrogen production were pH 6.0 and 37 degrees C, respectively. The volumetric loading of the bioreactor for hydrogen production can be as high as 650 mmol hydrogen/L culture with a yield at approximately 2.0 mol hydrogen/mol glucose. Acetate and butyrate made up approximately 80% of the total metabolites. The inhibitory effect from the two metabolites on the hydrogen production process was investigated. Butyrate at a concentration higher than 13 g/L significantly inhibited not only cell growth but also hydrogen production (i.e., specific hydrogen production rate). Acetate appears to be less toxic than butyrate to the hydrogen production process. While significantly inhibiting cell growth, acetate hardly affected hydrogen production. Finally, the factors limiting cultivation performance were discussed and possible strategies for enhancing the production of hydrogen were proposed.
我们证明了使用丙酮丁醇梭菌悬浮培养物作为生物催化剂连续生产氢气的补料分批操作的可行性。当前用于氢气生产的培养系统的最佳操作pH值和温度分别为pH 6.0和37摄氏度。用于氢气生产的生物反应器的体积负荷可高达650 mmol氢气/升培养物,产率约为2.0摩尔氢气/摩尔葡萄糖。乙酸盐和丁酸盐约占总代谢产物的80%。研究了这两种代谢产物对氢气生产过程的抑制作用。浓度高于13 g/L的丁酸盐不仅显著抑制细胞生长,还抑制氢气生产(即比氢气生产速率)。乙酸盐对氢气生产过程的毒性似乎比丁酸盐小。虽然乙酸盐显著抑制细胞生长,但几乎不影响氢气生产。最后,讨论了限制培养性能的因素,并提出了提高氢气产量的可能策略。