Abstract
The treatability of dilute wastewater by a UASB reactor was evaluated. After being seeded with digested sewage sludge, a 110-l reactor was operated at 25 °C under continuous feeding with synthetic wastewater having a COD of 300 mg/l for over 700 d. The hydraulic retention time (HRT) was successfully decreased in steps to 9 h (0.73 kg COD/m3/d). Granules began to be observed after the reactor had been in operation for 9 months. At an HRT of 9 h, the following results were obtained: soluble and total COD removal, 81±5% and 73±7%, respectively; methane production, 212 Nl/kg COD removed and 153 Nl/kg COD added; substrate conversion, 0.24 kg COD removed/kg VSS/d.
Original language | English |
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Pages (from-to) | 179-184 |
Number of pages | 6 |
Journal | Journal of Fermentation and Bioengineering |
Volume | 83 |
Issue number | 2 |
DOIs | |
Publication status | Published - 1997 Jan 1 |
Keywords
- COD mass balance
- UASB reactor
- anaerobic process
- developing countries
- granule size distribution
- sewage
- sludge retention time
- treatment performance
ASJC Scopus subject areas
- Biotechnology
- Applied Microbiology and Biotechnology