Li Dong, Cui Ya-Qian, Zhao Shi-Xun, Liu Zhi-Cheng, Zhang Jie
Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Architecture and Civil Engineering of Beijing University of Technology, Beijing 100124, China.
State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, Harbin 150090, China.
Huan Jing Ke Xue. 2018 Nov 8;39(11):5074-5080. doi: 10.13227/j.hjkx.201805005.
Outside the municipal waste water treatment plant(WWTP) which located in Mentougou District, Beijing, the effluent of the anoxic/oxic(A/O) phosphorus removal process served as the substrate to operate a completely autotrophic nitrogen removal over nitrite(CANON) filter reactor.. After the reactor was successfully activated, glucose was added to the influent as the organic carbon source. The simultaneous partial nitrification, anaerobic ammonium oxidation (ANAMMOX), and denitrification (SNAD) process was started to study the effect of SNAD filter on sewage treatment. The results showed that from 119 d to 128 d, the ammonia removal rate of the CANON process was more than 95%, and the maximum total nitrogen concentration in the effluent was 13.0 mg·L. Total nitrogen concentration surpassed the 1A level of the Integrated Discharge Standard of Water Pollutants applied in Beijing City. The SNAD process was started by adding glucose to the influent at 129 d. The total nitrogen removal rate of this process was about 85% at 133-187 d, and the total nitrogen concentration in the effluent was 5.5-7.3 mg·L. The filter plugged up at 195 d, and backwash was utilized at 196 d. During the subsequent 30 d, the total nitrogen removal rate of the reactor was greater than 85%, and the total nitrogen concentration in the effluent remained at 6.2-7.2 mg·L. Compared with the CANON process, the SNAD process improved the total nitrogen removal rate and reduced the total nitrogen concentration of the effluent by 6 mg·L. The ammonia and total nitrogen concentrations in effluent satisfied the 1A level of the Integrated Discharge Standard of Water Pollutants.
在北京门头沟区的城市污水处理厂(WWTP)外,以缺氧/好氧(A/O)除磷工艺的出水为底物,运行一个亚硝酸盐型完全自养脱氮(CANON)滤池反应器。反应器成功启动后,向进水添加葡萄糖作为有机碳源。启动了同步短程硝化、厌氧氨氧化(ANAMMOX)和反硝化(SNAD)工艺,以研究SNAD滤池对污水处理的效果。结果表明,在第119天至128天,CANON工艺的氨去除率超过95%,出水最大总氮浓度为13.0mg·L。总氮浓度超过北京市适用的《水污染物综合排放标准》一级A标准。在第129天向进水添加葡萄糖启动SNAD工艺。在第133天至187天,该工艺的总氮去除率约为85%,出水总氮浓度为5.5 - 7.3mg·L。在第195天滤池堵塞,于第196天进行反冲洗。在随后的30天里,反应器的总氮去除率大于85%,出水总氮浓度保持在6.2 - 7.2mg·L。与CANON工艺相比,SNAD工艺提高了总氮去除率,使出水总氮浓度降低了6mg·L。出水氨氮和总氮浓度均满足《水污染物综合排放标准》一级A标准。