Fermentation process for continuous production of succinic acid in a fibrous bed bioreactor

被引:23
|
作者
Yan, Qiang [1 ,2 ]
Zheng, Pu [1 ]
Tao, Sheng-Tao [1 ,2 ]
Dong, Jin-Jun [1 ]
机构
[1] Jiangnan Univ, Sch Biotechnol, Minist Educ, Key Lab Ind Biotechnol, Wuxi 214122, Jiangsu, Peoples R China
[2] Jiangnan Univ, State Key Lab Food Sci & Technol, Wuxi 214122, Jiangsu, Peoples R China
关键词
Actinobacillus succinogenes; Succinic acid; Bioprocess design; Bioreactors; Fermentation; Immobilized cells; ACTINOBACILLUS-SUCCINOGENES; BATCH; BIOTECHNOLOGY; CULTURES;
D O I
10.1016/j.bej.2014.08.002
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Succinic acid (SA) was produced from Actinobacillus succinogenes with high cell density by continuous fermentation using fibrous bed bioreactor (FBB). The effects of feeding glucose concentration, dilution rate, and pH on continuous production of SA were examined to achieve an efficient and economical bioprocess. The optimum feeding glucose concentration, dilution rate, and pH were 80 g/L, 0.051/h, and 6.0-6.5, respectively. A SA concentration of 55.3 +/- 0.8 g/L, productivity of 2.77 +/- 0.04 g/L/h, and yield of 0.8 +/- 0.02 g/g were obtained, and the continuous fermentation exhibited long-term stability for as long as 18 days (440 h) with no obvious fluctuations in both SA and biomass levels. The Jerusalimsky equation for the specific rate of SA production presented the inhibition phenomenon of the product, demonstrating that 60 g/L SA might be a critical concentration in this continuous FBB system. The results obtained could be beneficial for future fermentor designs and improvements in SA production. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:92 / 98
页数:7
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