Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing 100124, China.
School of Water Resources and Environmental Engineering, East China Institute of Technology, Nanchang 330013, China.
J Environ Sci (China). 2016 Apr;42:267-274. doi: 10.1016/j.jes.2015.09.006. Epub 2015 Dec 7.
The objective of this study was to investigate the nitritation performance in a biofilm reactor for treating domestic wastewater. The reactor was operated in continuous feed mode from phases 1 to 3. The dissolved oxygen (DO) was controlled at 3.5-7 mg/L throughout the experiment. The biofilm reactor showed excellent nitritation performance after the inoculation of nitrifying sludge, with the hydraulic retention time being reduced from 24 to 7 hr. Above 90% nitrite accumulation ratio (NAR) was maintained in phase 1. Afterwards, nitratation occurred with the low NH4(+)-N concentration in the reactor. The improvement of NH4(+)-N concentration to 20-35 mg/L had a limited effect on the recovery of nitritation. However, nitritation recovered rapidly when sequencing batch feed mode was adopted in phase 4, with the effluent NH4(+)-N concentration above 7 mg/L. The improvement of ammonia oxidizing bacteria (AOB) activity and the combined inhibition effect of free ammonia (FA) and free nitrous acid (FNA) on the nitrite oxidizing bacteria (NOB) were two key factors for the rapid recovery of nitritation. Sludge activity was obtained in batch tests. The results of batch tests had a good relationship with the long term operation performance of the biofilm reactor.
本研究旨在考察生物膜反应器处理生活污水的亚硝化性能。该反应器在 1 至 3 阶段连续进料模式下运行。整个实验过程中,溶解氧(DO)控制在 3.5-7mg/L。接种硝化污泥后,生物膜反应器表现出优异的亚硝化性能,水力停留时间从 24 小时缩短至 7 小时。在第 1 阶段,亚硝态氮积累率(NAR)保持在 90%以上。随后,由于反应器中 NH4(+)-N 浓度较低,发生了硝化作用。将 NH4(+)-N 浓度提高到 20-35mg/L 对恢复亚硝化作用的效果有限。然而,在第 4 阶段采用序批式进料模式时,亚硝化作用迅速恢复,出水 NH4(+)-N 浓度高于 7mg/L。氨氧化菌(AOB)活性的提高和游离氨(FA)与游离亚硝酸(FNA)对亚硝酸氧化菌(NOB)的联合抑制作用是亚硝化作用迅速恢复的两个关键因素。在批量试验中获得了污泥活性。批量试验结果与生物膜反应器的长期运行性能有很好的关系。