Abstract
The two-stage and two-phase anaerobic process (TSTP) composed of hydrolytic acidification reactor, first-order and second-order external circulation anaerobic reactors (EC) was taken to treat methanol wastewater. Test results show that TSTP process is quick start-up in 51 d, and the maximum VFA of hydrolytic acidification reactor effluent reaches 876 mg/L. Under the condition of volume loading of 6.56 kgCOD/m3·d, COD removal rate of the first-order EC reactor is about 85%, and under the condition of volume loading of 1.02 kgCOD/m3·d, COD removal rate of the second-order EC reactor is about 50%. When the inflow COD of TSTP process is between 7000-11000 mg/L, its effluent COD is lower than 600 mg/L. In the biological conversion process of methanol into methane, the production of acetic acids as an intermediate product can be ignored and the direct production of methane from methanol is predominant.
| Original language | English |
|---|---|
| Pages (from-to) | 65-69 |
| Number of pages | 5 |
| Journal | Journal of Harbin Institute of Technology (New Series) |
| Volume | 17 |
| Issue number | 1 |
| State | Published - Feb 2010 |
Keywords
- External circulation anaerobic reactor (EC)
- Hydrolytic acidification reactor
- Methanol wastewater
- Two-stage and two-phase anaerobic process (TSTP)
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