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
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