Department of Environmental Health Engineering, School of Public Health, Tehran University of Medical Sciences, Tehran, Iran.
Department of Environmental Engineering (Water Resources), Science and Research Branch, Faculty of Environment and Energy (FEE), Islamic Azad University, Tehran, Iran.
J Environ Health Sci Eng. 2014 Nov 13;12(1):134. doi: 10.1186/s40201-014-0134-2. eCollection 2014.
Simultaneous nitrogen, phosphorous and COD removal in a pilot-scale enhanced Sequencing Batch Reactor (eSBR) was investigated.
The reactor consisted of a pre-anoxic zone and internal recycle and was fed with synthetic wastewater. The study was performed by operating the reactor in 6-hour cycles in three different operational modes during a time frame of 279 days.
Under the best operational conditions, the average removal rate of COD, TN, and TP were obtained as 93.52, 88.31, and 97.56%, respectively.
A significant denitrifying phosphorus removal (more than 80%) occurred at run1 and 3 which started the cycle under anoxic condition.
在中试规模的强化序批式反应器(eSBR)中同时去除氮、磷和 COD。
该反应器由预缺氧区和内部循环组成,并使用合成废水进行进料。在 279 天的时间框架内,通过在三种不同操作模式下以 6 小时的周期运行反应器来进行研究。
在最佳操作条件下,COD、TN 和 TP 的平均去除率分别为 93.52%、88.31%和 97.56%。
在运行 1 和 3 中发生了显著的反硝化除磷(超过 80%),这是在缺氧条件下开始循环的结果。