Trojanowicz Karol, Plaza Elzbieta, Trela Jozef
Department of Sustainable Development, Environmental Science and Engineering, Royal Institute of Technology (KTH), Teknikringen 76, 100-44, Stockholm, Sweden E-mail:
Water Sci Technol. 2016;73(4):761-8. doi: 10.2166/wst.2015.551.
Process of partial nitritation-anammox for mainstream wastewater at low temperature was run in a pilot scale moving bed biofilm reactor (MBBR) system for about 300 days. The biofilm history in the reactor was about 3 years of growth at low temperature (down to 10 °C). The goal of the studies presented in this paper was to achieve effective partial nitritation-anammox process. Influence of nitrogen loading rate, hydraulic retention time, aeration strategy (continuous versus intermittent) and sludge recirculation (integrated fixed-film activated sludge (IFAS) mode) on deammonification process' efficiency and microbial activity in the examined system was tested. It was found that the sole intermittent aeration strategy is not a sufficient method for successful suppression of nitrite oxidizing bacteria in MBBR. The best performance of the process was achieved in IFAS mode. The highest recorded capacity of ammonia oxidizing bacteria and anammox bacteria in biofilm was 1.4 gN/m(2)d and 0.5 gN/m(2)d, respectively, reaching 51% in nitrogen removal efficiency.
在中试规模的移动床生物膜反应器(MBBR)系统中运行低温主流废水的部分亚硝化-厌氧氨氧化工艺约300天。反应器中的生物膜生长历史约为3年,生长温度较低(低至10℃)。本文所呈现研究的目标是实现有效的部分亚硝化-厌氧氨氧化工艺。测试了氮负荷率、水力停留时间、曝气策略(连续曝气与间歇曝气)和污泥回流(一体化固定膜活性污泥(IFAS)模式)对所研究系统中脱氨工艺效率和微生物活性的影响。结果发现,仅采用间歇曝气策略不足以成功抑制MBBR中的亚硝酸盐氧化细菌。该工艺在IFAS模式下表现最佳。生物膜中记录到的氨氧化细菌和厌氧氨氧化细菌的最高容量分别为1.4 gN/m²·d和0.5 gN/m²·d,脱氮效率达到51%。