厌氧氨氧化菌
硝化作用
废水
生物膜
移动床生物膜反应器
生物反应器
化学
铵
细菌
环境化学
污水处理
氨
氮气
制浆造纸工业
环境工程
反硝化
环境科学
生物
反硝化细菌
生物化学
有机化学
工程类
遗传学
作者
Rong Chen,Yoko Takemura,Yuan Liu,Jiayuan Ji,Satoshi Sakuma,Kengo Kubota,Haiyuan Ma,Yu-You Li
出处
期刊:ACS Sustainable Chemistry & Engineering
[American Chemical Society]
日期:2018-12-09
卷期号:7 (1): 1353-1361
被引量:36
标识
DOI:10.1021/acssuschemeng.8b05055
摘要
The stable operation of partial nitrification and anammox (PNA) process is a challenge in nitrogen removal from extremely low-strength ammonia wastewater like sewage mainstream. A moving bed reactor with functional carriers (30% filling rate) was developed to treat a synthetic influent with 50 mg/L ammonia. The long-term operation results showed nitrogen removal efficiencies of 71.7 ± 9.1% have been stably obtained under a relatively short hydraulic retention time of 2 h. Microbial analysis revealed anammox bacteria and ammonium oxidizing bacteria (AOB) with 29.7% and 6.32% abundance were the two most dominant bacteria in the reactor. Carriers largely retained slow-growing anammox bacteria in their hollow space and established a sandwich-like biofilm structure of co-immobilization of anammox bacteria and AOB. The anammox activity was much higher in carrier biofilms than in suspended flocs, while, for the AOB activity, the situation was reversed. Correspondingly, a fluorescent in situ hybridization analysis illustrated the active cell fractions of anammox bacteria and AOB in carrier biofilms were 63.7% and 4.8%, and 2.7% and 61.4% in suspended flocs. Biofilm formation and dissolved oxygen control were deemed to be the two key factors affecting the optimal co-immobilization of anammox bacteria and AOB, which guaranteed the efficient PNA.
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