کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
150804 | 456457 | 2011 | 5 صفحه PDF | دانلود رایگان |
The use of different carbon sources (ethanol, acid-fermented primary sludge centrate, acid-fermented secondary sludge centrate, glycerol and landfill leachate) in heterotrophic denitrification from nitrite (denitritation) was studied in a sequencing batch reactor, operated without pH control. Complete denitritation of a high-strength nitrite wastewater was achieved using these organic carbon sources with the exception of fermented secondary sludge centrate. Loading rates around 0.2 g N L−1 d−1 were obtained for glycerol, landfill leachate and ethanol after a short start-up period of 20 days. The maximum specific nitrite removal rate of 0.25 g N g−1 VSS d−1 was achieved for glycerol, while values between 0.13 and 0.17 g N g−1 VSS d−1 were obtained using ethanol, landfill leachate and fermented primary sludge centrate. The COD/N ratio consumed varied between 3.0 for ethanol and 8.8 for landfill leachate. The denitritation rates and the required COD/N ratio for each carbon source are reported for the first time – they can be used for the scale-up of the denitritation process.
► SBR operation for heterotrophic denitrification from nitrite (denitritation).
► First description of SBR operation for denitritation with alternative carbon sources.
► Denitritation with glycerol, ethanol, landfill leachate and fermented primary sludge.
► Denitritation rates and required COD/N ratio for each carbon source are reported.
► The reported data can be used for the scale-up of the denitritation process.
Journal: Chemical Engineering Journal - Volume 172, Issues 2–3, 15 August 2011, Pages 994–998