Liu Chun, Wang Cong-Cong, Chen Xiao-Xuan, Zhang Jing, Zhang Rui-Na, Zhang Lei
Pollution Prevention Biotechnology Laboratory of Hebei Province, School of Environmental Science and Engineering, Hebei University of Science and Technology, Shijiazhuang 050018, China.
Huan Jing Ke Xue. 2019 Feb 8;40(2):754-760. doi: 10.13227/j.hjkx.201807085.
The microbubble-aerated biofilm reactor as a new treatment process combines microbubble aeration technology with aerobic biological treatment. A microbubble aerated biofilm reactor was used in this study to treat low C/N ratio wastewater at a low air/water ratio. The process and performance of biological nitrogen removal were investigated, and the functional bacterial populations for nitrogen removal in the biofilm were analyzed. The results showed that the biological nitrogen removal process was converted from simultaneous nitrification-denitrification to simultaneous partial nitrification, ANAMMOX and denitrification (SNAD) processes when DO concentration was controlled by an air/water ratio of lower than 1:2 and the influent C/N ratio was reduced. As a result, the efficient biological nitrogen removal performance was achieved when treating low C/N ratio wastewater. When the DO concentration was lower than 1.0 mg·L and the influent C/N ratio was 1:2.8, the SNAD process became dominant for biological nitrogen removal. In this case, the average total nitrogen (TN) removal efficiency was 76.3%, and the average TN loading rate removed was 1.42 kg·(m·d). In addition, it was estimated that 86.0% of TN removal was attributed to the ANAMMOX process. The relative abundances of ammonia-oxidizing bacteria populations and ANAMMOX bacteria populations in the biofilm increased gradually, while the relative abundances of nitrite-oxidizing bacteria populations and denitrifying bacteria populations decreased gradually, with a decrease in influent C/N ratio. The variation of functional bacterial populations for nitrogen removal was consistent with the conversion of nitrogen removal process to SNAD process.
微气泡曝气生物膜反应器作为一种新型处理工艺,将微气泡曝气技术与好氧生物处理相结合。本研究采用微气泡曝气生物膜反应器以低气水比处理低C/N比废水。研究了生物脱氮的工艺和性能,并分析了生物膜中脱氮功能细菌种群。结果表明,当气水比控制在低于1:2且进水C/N比降低时,生物脱氮过程从同步硝化反硝化转变为同步部分硝化、厌氧氨氧化和反硝化(SNAD)过程。因此,在处理低C/N比废水时实现了高效的生物脱氮性能。当溶解氧(DO)浓度低于1.0mg·L且进水C/N比为1:2.8时,SNAD过程成为生物脱氮的主导过程。在此情况下,平均总氮(TN)去除效率为76.3%,平均TN去除负荷为1.42kg·(m·d)。此外,据估计86.0%的TN去除归因于厌氧氨氧化过程。随着进水C/N比的降低,生物膜中氨氧化细菌种群和厌氧氨氧化细菌种群的相对丰度逐渐增加,而亚硝酸盐氧化细菌种群和反硝化细菌种群的相对丰度逐渐降低。脱氮功能细菌种群的变化与脱氮过程向SNAD过程的转变一致。