Department of Environmental Science and Engineering, Fudan University, Room 2026, Environment Building, 2005 Songhu Road, Yangpu District, Shanghai, 200433, China.
Bioprocess Biosyst Eng. 2020 Jul;43(7):1241-1252. doi: 10.1007/s00449-020-02319-3. Epub 2020 Mar 12.
In this research, a novel packed anoxic/oxic moving bed biofilm reactor (MBBR) was established to achieve high-organic matter removal rates, despite the carbon/nitrogen (C/N) ratio of 2.7-5.1 in the influent. Simultaneous nitrification-denitrification (SND) was investigated under a long sludge retention time of 104 days. The system exhibited excellent performance in pollutant removal, with chemical oxygen demand and total nitrogen (TN) enhanced to 93.6-97.4% and 34.4-60%, respectively. Under low C/N conditions, the nitrogen removal process of A/O MBBR system was mainly achieved by anaerobic denitrification. The increase of C/N ratio enhanced SND rate of the aerobic section, where dissolved oxygen was maintained at the range of 4-6 mg/L, and resulted in higher TN removal efficiency. The microbial composition and structures were analyzed utilizing the MiSeq Illumina sequencing technique. High-throughput pyrosequencing results indicated that the dominant microorganisms were Proteobacteria and Bacteroidetes at the phylum level, which contributes to the removal of organics matters. In the aerobic section, abundances of Nitrospirae (1.12-29.33%), Burkholderiales (2.15-21.38%), and Sphingobacteriales (2.92-11.67%) rose with increasing C/N ratio in the influent, this proved that SND did occur in the aerobic zone. As the C/N ratio of influent increased, the SND phenomenon in the aerobic zone of the system is the main mechanism for greatly improving the removal rate of TN in the aerobic section. The C/N ratio in the aerobic zone is not required to be high to exhibit good TN removal performance. When C/NH and C/TN in the aerobic zone were higher than 2.29 and 1.77, respectively, TN removal efficiency was higher than 60%, which means that carbon sources added to the reactor could be saved. This study would be vital for a better understanding of microbial structures within a packed A/O MBBR and the development of cost-efficient strategies for the treatment of low C/N wastewater.
在这项研究中,建立了一种新型的缺氧/好氧移动床生物膜反应器(MBBR),即使进水的碳氮比(C/N)为 2.7-5.1,也能实现高有机物去除率。在 104 天的长污泥停留时间下研究了同时硝化反硝化(SND)。该系统在污染物去除方面表现出优异的性能,化学需氧量和总氮(TN)分别提高到 93.6-97.4%和 34.4-60%。在低 C/N 条件下,A/O-MBBR 系统的脱氮过程主要通过厌氧反硝化实现。C/N 比的增加提高了好氧段的 SND 速率,好氧段的溶解氧保持在 4-6mg/L 范围内,从而提高了 TN 去除效率。利用 MiSeq Illumina 测序技术分析了微生物组成和结构。高通量焦磷酸测序结果表明,在门水平上,优势微生物主要为变形菌门和拟杆菌门,这有助于去除有机物。在好氧段,随着进水 C/N 比的增加,硝化螺旋菌属(1.12-29.33%)、伯克霍尔德氏菌科(2.15-21.38%)和鞘脂单胞菌科(2.92-11.67%)的丰度增加,这证明了 SND 确实发生在好氧区。随着进水 C/N 比的增加,系统好氧区的 SND 现象是大幅提高好氧段 TN 去除率的主要机制。好氧区的 C/N 比不需要很高就能表现出良好的 TN 去除性能。当好氧区的 C/NH 和 C/TN 分别高于 2.29 和 1.77 时,TN 去除效率高于 60%,这意味着可以节省添加到反应器中的碳源。本研究对于更好地了解填充 A/O-MBBR 中的微生物结构以及开发高效、经济的低 C/N 废水处理策略具有重要意义。