Environ Technol. 2014 Mar-Apr;35(5-8):523-31. doi: 10.1080/09593330.2013.796006.
Anaerobic ammonium oxidation (ANAMMOX) is an innovative process for the treatment of ammonia-contaminated waters. ANNAMOX is usually preceded by a nitrifying step in which ammonia is partially oxidized to nitrite. The effectiveness of the overall process depends on control of the nitrification and creation of a suitable influent for ANAMMOX. In this work, impacts of ammonia concentration and loading rate on partial nitrification and composition of the resulting effluent were investigated in continuous stirred tank (CSTR) and biofilm reactors fed with various ammonia concentrations (17.6-61.5 mM; 299-1045 ppm). Regardless of ammonia concentration, loading rates from 3.1 to 5.4mM/h in the CSTR and 6.4-12.1 mM/h in the biofilm reactor generated effluents with nitrite to ammonia ratios of 1.2 +/- 0.3 (suitable ANAMMOX influent). Under these conditions, the highest ammonia loading and nitrite production rates in the CSTR and biofilm reactors were 5.4 and 2.5 mM/h (HRT: 3.7 h) and 12.1 and 6.5 mM/h (HRT: 1.6 h), respectively. Results reveal that ammonia loading rate can be used effectively to achieve suitable ANAMMOX influent without the need for precise control of dissolved oxygen (DO). Considering the difficulty in regulating DO in large-scale systems and the need for the nitrifying process to be flexible with respect to various ammonia concentrations, the loading rate appears to be a practical option to control partial nitrification. Verifying the range of ammonia loading rates that generate ANAMMOX influent allows operation of the nitrifying step with any level of ammonia in the feed, with the proper loading rate achieved through adjustment of hydraulic residence time.
厌氧氨氧化(ANAMMOX)是一种处理含氨污水的创新工艺。ANAMMOX 通常以前硝化步骤为先导,其中氨部分氧化为亚硝酸盐。整个过程的有效性取决于硝化的控制和 ANAMMOX 合适的进水条件的创造。在这项工作中,采用连续搅拌槽(CSTR)和生物膜反应器,研究了不同氨浓度(17.6-61.5mM;299-1045ppm)下氨浓度和负荷率对部分硝化和出水组成的影响。无论氨浓度如何,CSTR 的负荷率为 3.1-5.4mM/h,生物膜反应器的负荷率为 6.4-12.1mM/h,都能产生亚硝酸盐与氨的比值为 1.2±0.3 的出水(适合 ANAMMOX 的进水)。在这些条件下,CSTR 和生物膜反应器的最高氨负荷和亚硝酸盐生成速率分别为 5.4 和 2.5mM/h(HRT:3.7h)和 12.1 和 6.5mM/h(HRT:1.6h)。结果表明,氨负荷率可有效地用于实现适合 ANAMMOX 的进水,而无需精确控制溶解氧(DO)。考虑到在大型系统中调节 DO 的困难以及硝化过程需要灵活适应各种氨浓度,负荷率似乎是控制部分硝化的一种实用选择。验证产生 ANAMMOX 进水的氨负荷率范围可以使硝化步骤在进料中具有任何水平的氨运行,通过调整水力停留时间来达到适当的负荷率。