Acetone-butanol-ethanol fermentation in a continuous and closed-circulating fermentation system with PDMS membrane bioreactor

被引:53
作者
Chen, Chunyan [1 ]
Xiao, Zeyi [1 ]
Tang, Xiaoyu [2 ]
Cui, Haidi [1 ]
Zhang, Junqing [1 ]
Li, Weijia [1 ]
Ying, Chao [1 ]
机构
[1] Sichuan Univ, Sch Chem Engn, Chengdu 610065, Peoples R China
[2] Minist Agr, Biogas Inst, Biomass Energy Technol Res Ctr, Chengdu 610041, Peoples R China
基金
中国国家自然科学基金;
关键词
ABE fermentation; PDMS membrane bioreactor; Butanol; Pervaporation; CLOSTRIDIUM-ACETOBUTYLICUM; COMPOSITE MEMBRANES; BATCH FERMENTATION; PERVAPORATION; RECOVERY; SACCHARIFICATION; BEIJERINCKII; BROTH;
D O I
10.1016/j.biortech.2012.10.077
中图分类号
S2 [农业工程];
学科分类号
082806 [农业信息与电气工程];
摘要
Acetone-butanol-ethanol (ABE) fermentation by combining a PDMS membrane bioreactor and Clostridium acetobutylicum was studied, and a long continuous and closed-circulating fermentation (CCCF) system has been achieved. Two cycles of experiment were conducted, lasting for 274 h and 300 h, respectively. The operation mode of the first cycle was of fermentation intermittent coupling with pervaporation, and the second cycle was of continuous coupling. The average cell weight, glucose consumption rate, butanol productivity and butanol production of the first cycle were 1.59 g L-1, 0.63 g L-1 h(-1), 0.105 g L-1 h(-1) and 28.03 g L-1, respectively. Correspondingly, the four parameters of the second cycle were 1.68 g L-1, 1.12 g L-1 h(-1), 0.205 g L-1 h(-1) and 61.43 g L-1, respectively. The results indicate the fermentation behaviors under continuous coupling mode were superior to that under intermittent coupling mode. Besides, two peak values were observed in the time course profiles, which means the microorganism could adapt the long CCCF membrane bioreactor system. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:246 / 251
页数:6
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