• Title of article

    Overcoming propionic acid inhibition of hydrogen fermentation by temperature shift strategy

  • Author/Authors

    Sivagurunathan، نويسنده , , Periyasamy and Sen، نويسنده , , Biswarup and Lin، نويسنده , , Chiu-Yue، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2014
  • Pages
    10
  • From page
    19232
  • To page
    19241
  • Abstract
    A novel temperature shift strategy has been proposed to overcome an inhibition on hydrogen fermentation of beverage industry wastewater (BW) due to the accumulation of propionic acid (HPr) during continuous reactor operation. The continuous performance at constant pH 5.5, temperature 37 °C and hydraulic retention time (HRT) 8 h with BW concentration of 20 g/Lhexose-equivalent in a stirred tank reactor (2 L) showed an accumulation of HPr to 2.36 g/L leading to a drop in hydrogen production rate (HPR) from 10 to 8.5 L L−1 d−1. To overcome the HPr inhibition, a temperature shift (from 37 °C) to 45 °C for 8 h was applied. This significantly improved the inhibited HPR and HY to 13.6 L L−1 d−1 and 1.68 mol-H2 mol−1 hexose, respectively, with a simultaneous reduction in the HPr concentration to 0.7 g/L. Microbial community analysis based on PCR-DGGE after temperature shift revealed the non-dominance of Selenomonas lacticifex and Bifidobacterium catenulatum (involved in HPr formation), and dominance of hydrogen producing bacteria namely Clostridium butyricum, Clostridium perfringenes, Clostridium acetobutylicum, and Ethanoligenens harbinense. This study demonstrated that temperature shift strategy could overcome the HPr inhibition and significantly improve the hydrogen fermentation of an industrial wastewater.
  • Keywords
    Beverage wastewater , Bifidiobacterium , Continuous stirred-tank reactor , Selenomonas , temperature shift
  • Journal title
    International Journal of Hydrogen Energy
  • Serial Year
    2014
  • Journal title
    International Journal of Hydrogen Energy
  • Record number

    1870842