Abstract
Biological treatment of sulfate-laden wastewater consists of two separate reactors to reduce sulfate to sulfide by sulfate-reducing bacteria (SRB) and to oxidize sulfide to sulfur (S0) by sulfide oxidation bacteria (SOB). To have SRB+SOB in a single reactor faced difficulty of low S0 conversion. This study for the first time revealed that dissolved oxygen (DO) level can be used to manipulate SRB+SOB reactions in a single reactor. This work demonstrated successful operation of an integrated SRB+SOB reactor under micro-aerobic condition. At DO=0.10-0.12mgl-1, since the activities of SOB were enhanced by limited oxygen, the removal efficiency for sulfate reached 81.5% and the recovery of S0 peaked at 71.8%, higher than those reported in literature. At increased DO, chemical oxidation of sulfide with molecular oxygen competed with SOB so conversion of S0 started to decline. At DO>0.30mgl-1 activities of SRB were inhibited, leading to failure of the SRB+SOB reactor.
| Original language | English |
|---|---|
| Pages (from-to) | 517-521 |
| Number of pages | 5 |
| Journal | Bioresource Technology |
| Volume | 116 |
| DOIs | |
| State | Published - Jul 2012 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Elemental sulfur recovery
- Integrated process
- Micro-aerobic condition
- Sulfate reducing
- Sulfide oxidizing
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