4.8 Article

Performance of batch, fed-batch, and continuous A-B-E fermentation with pH-control

期刊

BIORESOURCE TECHNOLOGY
卷 102, 期 5, 页码 4241-4250

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.biortech.2010.12.078

关键词

A-B-E fermentation; pH control; Batch reactor; Fed-batch reactor; Chemostat

资金

  1. DOE [DE-EE0003116]
  2. Connecticut Department of Economic and Community Development
  3. Directorate For Engineering
  4. Div Of Chem, Bioeng, Env, & Transp Sys [827800] Funding Source: National Science Foundation

向作者/读者索取更多资源

Batch, fed-batch, and continuous A-B-E fermentations were conducted and compared with pH controlled at 4.5, the optimal range for solvent production. While the batch mode provides the highest solvent yield, the continuous mode was preferred in terms of butanol yield and productivity. The highest butanol yield and productivity found in the continuous fermentation at dilution rate of 0.1h(-1) were 0.21 g-butanol/g-glucose and 0.81 g/L/h, respectively. In the continuous and fed-batch fermentation, the time needed for passing acidogenesis to solventogenesis was an intrinsic hindrance to higher butanol productivity. Therefore, a low dilution rate is suggested for the continuous A-B-E fermentation, while the fed-batch mode is not suggested for solvent production. While 3:6:1 ratio of acetone, butanol, and ethanol is commonly observed from A-B-E batch fermentation by Clostridium acetobutylicum when the pH is uncontrolled, up to 94% of the produced solvent was butanol in the chemostat with pH controlled at 4.5. (C) 2010 Elsevier Ltd. All rights reserved.

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