摘要
在好氧连续曝气方式下采用自生生物动态膜反应器处理低C/N污水,水力停留时间为5h,膜通量为17~19L/(m^2·h),COD/NH4^+-N在0.56~2.22,COD去除率在起始阶段达70%左右,运行稳定后,下降到40%左右;NH4^+-N的去除率一直稳定在60.0%左右。在NH4^+-N的氧化过程中,NH^4+-N除被生物利用外,大部分被转化为NOF-N(出水中NO3^-N浓度非常低),亚硝化率平均达到94%。
Under aerobic condition, a self-forming dynamic membrane bioreactor was used for the treatment of septic tank wastewater at HRT=5 h, the membrane flux=17-19 L/(m2 · h) and the COD/NH4^+-N= 0.56-2.22. The removal efficiency of COD was 70% initially and decreased to 40% later. The NH4^+-N removal was about 60.0%. A major part of NH4^+ -N was oxidized to nitrite as evidenced by a low nitrate level in the effluent while the nitrite level increased in the reactor.
出处
《环境污染与防治》
CAS
CSCD
北大核心
2007年第4期293-296,共4页
Environmental Pollution & Control
基金
武汉市"十五"专项课题"景观水治理与中水回用技术研究及工程示范"(No.20046004069-05)。
关键词
自生生物动态膜反应器
低C/N
亚硝酸盐积累
Self-forming dynamic membrane bioreactor Low C/N ratio Nitrite accumulation