Denitritation of a high-strength nitrite wastewater in a sequencing batch reactor using different organic carbon sources

被引:49
|
作者
Tora, Josep A. [1 ,2 ]
Baeza, Juan A. [1 ]
Carrera, Julian [1 ]
Oleszkiewicz, Jan A. [2 ]
机构
[1] Univ Autonoma Barcelona, Dept Chem Engn, Escola Engn, E-08193 Barcelona, Spain
[2] Univ Manitoba, Dept Civil Engn, Winnipeg, MB R3T 5V6, Canada
关键词
Glycerol; Primary sludge; Leachate; Ethanol; Denitrification; SBR; NITROGEN REMOVAL; ANAEROBIC-DIGESTION; 2-SLUDGE SYSTEM; DENITRIFICATION; SLUDGE; NITRATE; ANAMMOX; RATIO; TEMPERATURE; INHIBITION;
D O I
10.1016/j.cej.2011.07.013
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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) VSSd(-1) was achieved for glycerol, while values between 0.13 and 0.17 g N g(-1) VSSd(-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. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:994 / 998
页数:5
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