Nitrogen removal from wastewater with a low COD/N ratio at a low oxygen concentration

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• 作者：Katarzyna Bernat^a ; ^{katarzyna.bernat@uwm.edu.pl} ; Dorota Kulikowska ; ^a ; ^{dorotak@uwm.edu.pl} ; Magdalena Zieliń ; ska^a ; ^{magdalena.zielinska@uwm.edu.pl} ; Agnieszka Cydzik-Kwiatkowska^a ; ^{agnieszka.cydzik@uwm.edu.pl} ; Irena Wojnowska-Barył ; a^a ; ^{irka@uwm.edu.pl}
• 关键词：Anaerobic sludge digester supernatant ; SBR ; Nitrification/denitrification ; COD removal ; Sludge production
• 刊名：Bioresource Technology
• 出版年：2011
• 出版时间：April 2011
• 年：2011
• 卷：102
• 期：7
• 页码：4913-4916
• 全文大小：222 K

文摘

The goal of the study was to determine the effectiveness of nitrification and denitrification and the kinetics of ammonia removal from a mixture of wastewater and anaerobic sludge digester supernatant in an SBR at limited oxygen concentration. In addition, the COD removal efficiency and sludge production were assessed.

In the SBR cycle alternating aerobic and anaerobic phases occurred; in the aeration phase the dissolved oxygen (DO) concentration was below 0.7 mg O₂/L. The low DO concentration did not inhibit ammonia oxidation–nitrification and the efficiency was ca. 96–98 % . However, a relatively high COD concentration in the effluent was detected. The values of K_m and V_max, calculated from the Michaelis–Menten equation, were 43 mg N–NH₄/L and 15.64 mg N–NH₄/L h, respectively. Activated sludge production was almost stable (0.62–0.66 g MLVSS/g COD). A high net biomass production resulted from a low specific biomass decay rate of 0.0015 d⁻¹.