摘要
生物慢滤工艺对COD、 SCOD和浊度去除率分别可达到49%、46%和77%;对COD、 SCOD和浊度,系统表层填料对COD、 SCOD和浊度的去除贡献较大;在填料5 cm以下装置对有机物和浊度的去除曲线斜率基本一致。生物慢滤池对于TP和溶解性磷酸盐可达到70%以上;系统对总氮去除率一般只有18.0%~30.0%,对氨氮去除率可达33%~67%。沿不同深度,磷和总氮的去除率基本呈不断增大的趋势;而氨氮的去除率呈现先增大后减小的规律。
The removal efficiencies of COD, SCOD and turbidity can reach 49%, 46%and 77%, respectively.The surface layer had larger contribution than the lower layers for COD, SCOD and turbidity removal.The curve slopes had no conspicuous variation for organic and turbidity removals behind 5 cm filler.The removal efficiencies of TP and dissolved phosphate can reach 70%.In addition, the removal rate of TN was only 18.0%~30.0%, however, the removal rate of ammonia nitrogen can reach 33%~67%.The TP and dissolved phosphate removal efficiencies had the increasing trend along the different depth, but for ammonia nitrogen removal, it was decreased first then increased.
出处
《广州化工》
CAS
2014年第23期72-74,116,共4页
GuangZhou Chemical Industry
基金
河南工业大学高层次人才基金(2012BS057)
河南工业大学科技创新人才培育计划项目基金(2014CXRC05)
关键词
生物慢滤工艺
景观水
处理效果
不同深度
slow biofiltration
landscape water
removal efficiencies
different depth