School of Energy and Environment, Southeast University, Nanjing 210096, China ; School of Sciences, China Pharmaceutical University, Nanjing 211198, China.
School of Energy and Environment, Southeast University, Nanjing 210096, China.
Saudi J Biol Sci. 2014 Jan;21(1):71-80. doi: 10.1016/j.sjbs.2013.06.003. Epub 2013 Jun 15.
In this study, the new anaerobic-anoxic/nitrifying/induced crystallization (A2N-IC) system was compared with anaerobic-anoxic/nitrifying (A2N) process to investigate nutrient removal performance under different influent COD and ammonia concentrations. Ammonia and COD removal rates were very stable in both processes, which were maintained at 84.9% and 86.6% when the influent ammonia varied from 30 mg L(-1) to 45 mg L(-1) and COD ranged from 250 mg L(-1) to 300 mg L(-1). The effluent phosphorus always maintained below 0.2 mg L(-1) in A2N-IC, whereas in A2N the effluent phosphorus concentration was 0.4-1.7 mg L(-1), demonstrating that A2N-IC is suitable to apply in a broader influent COD and ammonia concentration range. Under higher influent COD (300 mg L(-1)) or lower ammonia conditions (30 mg L(-1)), the main function of chemical induced crystallization was to coordinate better nutrient ratio for anoxic phosphorus uptake, whereas under high phosphorus concentration, it was to reduce phosphorus loading for biological system. Under the similar influent wastewater compositions, phosphorus release amounts were always lower in A2N-IC. To clarify the decrease procedure of phosphorus release in the A2N-IC, the equilibrium between chemical phosphorus removal and biological phosphorus removal in A2N-IC was analyzed by mass balance equations. During the long-term experiment, some undesirable phenomena were observed: the declining nitrification in post-aerobic tank and calcium phosphorus precipitation in the anaerobic tank. The reasons were analyzed; furthermore, the corresponding improvements were proposed. Nitrification effect could be enhanced in the post-aerobic tank, therefore ammonia removal rate could be increased; and biologically induced phosphorus precipitation could be inhibited by controlling pH at the anaerobic stage, so the phosphorus release and recovery could be improved.
在这项研究中,将新的厌氧-缺氧/硝化/诱导结晶(A2N-IC)系统与厌氧-缺氧/硝化(A2N)工艺进行比较,以研究不同进水 COD 和氨浓度下的营养去除性能。在两种工艺中,氨和 COD 的去除率都非常稳定,当进水氨从 30mg/L 变化到 45mg/L 时,COD 从 250mg/L 变化到 300mg/L 时,去除率分别保持在 84.9%和 86.6%。A2N-IC 的出水磷始终保持在 0.2mg/L 以下,而 A2N 的出水磷浓度为 0.4-1.7mg/L,表明 A2N-IC 适用于更宽的进水 COD 和氨浓度范围。在较高的进水 COD(300mg/L)或较低的氨条件(30mg/L)下,化学诱导结晶的主要功能是协调更好的缺氧磷吸收的营养比,而在高磷浓度下,它是为了减少生物系统的磷负荷。在类似的进水废水组成下,A2N-IC 中的磷释放量总是较低。为了阐明 A2N-IC 中磷释放的减少过程,通过质量平衡方程分析了 A2N-IC 中化学除磷和生物除磷之间的平衡。在长期实验中,观察到一些不良现象:后好氧池硝化作用下降和厌氧池钙磷沉淀。分析了原因,并提出了相应的改进措施。可以增强后好氧池的硝化作用,从而提高氨去除率;通过控制厌氧阶段的 pH 值,可以抑制生物诱导磷沉淀,从而改善磷的释放和回收。