†Advanced Wastewater Management Centre, The University of Queensland, St. Lucia, Brisbane, Queensland 4072, Australia.
‡Australian Water Quality Centre, Adelaide, South Australia 5000, Australia.
Environ Sci Technol. 2015 Aug 4;49(15):9176-84. doi: 10.1021/acs.est.5b02038. Epub 2015 Jul 17.
Nitrous oxide (N2O) emission data collected from wastewater treatment plants (WWTPs) show huge variations between plants and within one plant (both spatially and temporarily). Such variations and the relative contributions of various N2O production pathways are not fully understood. This study applied a previously established N2O model incorporating two currently known N2O production pathways by ammonia-oxidizing bacteria (AOB) (namely the AOB denitrification and the hydroxylamine pathways) and the N2O production pathway by heterotrophic denitrifiers to describe and provide insights into the large spatial variations of N2O fluxes in a step-feed full-scale activated sludge plant. The model was calibrated and validated by comparing simulation results with 40 days of N2O emission monitoring data as well as other water quality parameters from the plant. The model demonstrated that the relatively high biomass specific nitrogen loading rate in the Second Step of the reactor was responsible for the much higher N2O fluxes from this section. The results further revealed the AOB denitrification pathway decreased and the NH2OH oxidation pathway increased along the path of both Steps due to the increasing dissolved oxygen concentration. The overall N2O emission from this step-feed WWTP would be largely mitigated if 30% of the returned sludge were returned to the Second Step to reduce its biomass nitrogen loading rate.
污水处理厂(WWTP)收集的氧化亚氮(N2O)排放数据表明,不同工厂之间以及同一工厂内部(无论是空间上还是时间上)存在巨大差异。这些差异以及各种 N2O 产生途径的相对贡献尚不完全清楚。本研究应用了先前建立的 N2O 模型,该模型结合了氨氧化菌(AOB)的两种当前已知的 N2O 产生途径(即 AOB 反硝化和羟胺途径)和异养反硝化菌的 N2O 产生途径,以描述和深入了解分步进料式全规模活性污泥厂中 N2O 通量的大空间变化。该模型通过将模拟结果与 40 天的 N2O 排放监测数据以及工厂的其他水质参数进行比较来进行校准和验证。该模型表明,由于第二阶段的生物量比氮负荷率相对较高,导致该部分的 N2O 通量更高。结果进一步揭示了由于溶解氧浓度的增加,AOB 反硝化途径减少,NH2OH 氧化途径在两个阶段的流程中增加。如果将 30%的回流污泥回流到第二阶段以降低其生物量氮负荷率,则这种分步进料式 WWTP 的整体 N2O 排放量将大大减少。