• Title of article

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

  • Author/Authors

    Li، نويسنده , , Si-Yu and Srivastava، نويسنده , , Ranjan and Suib، نويسنده , , Steven L. and Li، نويسنده , , Yi and Parnas، نويسنده , , Richard S.، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2011
  • Pages
    10
  • From page
    4241
  • To page
    4250
  • Abstract
    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 0.1 h−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.
  • Keywords
    pH control , A–B–E fermentation , Batch reactor , Fed-batch reactor , chemostat
  • Journal title
    Bioresource Technology
  • Serial Year
    2011
  • Journal title
    Bioresource Technology
  • Record number

    1923784