DocumentCode :
3593930
Title :
Effect of Influent COD/N Ratio on Nitrous Oxide Production during Denitrification Using Different Electron Acceptors
Author :
Jingrong, Zhang ; Shuying, Wang
Author_Institution :
Key Lab. of Beijing for Water Quality Sci. & Water Environ. Recovery Eng., Beijing Univ. of Technol. Beijing, Beijing, China
Volume :
2
fYear :
2009
Firstpage :
511
Lastpage :
514
Abstract :
Nitrous oxide production in different influent COD/N ratios was investigated in lab-scale batch reactors using nitrite and nitrate as different electron acceptors, adding ethanol as external carbon source. The results showed that the maximum production of N2O was 1.91% (nitrite) and 0.48% (nitrate) of influent nitrogen, whereas 0.22% (nitrite) and 0.31% (nitrate) in the optimal influent COD/N ratio. Taking the effluent water quality and the minimum N2O production into account, the experiments suggested that the optimal influent COD/N ratio was 2.7-4.3 (nitrite) and 5.2-6.8 (nitrate). Furthermore, the results also demonstrated that the limited availability of electron donor resulted in nitrite accumulation which leaded to high N2O production. Hence, In order to reduce the production of N2O, it´s important to control influent COD/N ratio in an optimal value to avoid the accumulation of nitrite.
Keywords :
bioreactors; effluents; nitrogen compounds; wastewater treatment; water quality; N2O; denitrification; effluent; electron acceptors; ethanol addition; influent COD-N ratio; lab scale batch reactors; nitrous oxide production; water quality; Carbon dioxide; Electron emission; Ethanol; Inductors; Microorganisms; Nitrogen; Oxidation; Power engineering and energy; Production; Wastewater treatment; activated sludge; denitrification; influent COD/N ration; nitrate; nitrite; nitrous oxide;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
Energy and Environment Technology, 2009. ICEET '09. International Conference on
Print_ISBN :
978-0-7695-3819-8
Type :
conf
DOI :
10.1109/ICEET.2009.362
Filename :
5364600
Link To Document :
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