Abstract
The experiment was conducted to investigate continuous hydrogen production with lower cost and sulphate-rich wastewater treatment. In this paper, both anaerobic bio-treatment of sulphate-rich wastewater and hydrogen production were applied to construct a laboratory-scale combined sulphur cycle based system. The system consisted of two reactors, which were a photocatalytic reactor and an anaerobic bioreactor, respectively. In the anaerobic bioreactor, sulphate-reducing bacteria (SRB) converted SO42- to S 2-. The produced S2- yielded by SRB was further used as a sacrificial reagent to produce H2 in the photocatalytic reactor. Then, S 2- was changed into SO42-, which returned to the anaerobic bioreactor for treatment again. The present study highlighted an advantage compared with the conventional method, in that no extra S2-was added to the photocatalytic reactor, which reduced the total cost and realized continuous hydrogen production. The average COD removal efficiency was 79.6%.
| Original language | English |
|---|---|
| Pages (from-to) | 1297-1304 |
| Number of pages | 8 |
| Journal | Environmental Technology (United Kingdom) |
| Volume | 30 |
| Issue number | 12 |
| DOIs | |
| State | Published - Nov 2009 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Anaerobic bioreactor
- COD removal efficiency
- Hydrogen production
- SRB
- Sulphur cycle
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