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O3-BAF深度处理制革废水中沿程污染物降解规律
引用本文:余彬,刘锐,程家迪,范举红,李昌湖,冉坤,曹国华,陈吕军.O3-BAF深度处理制革废水中沿程污染物降解规律[J].环境科学,2013,34(3):974-978.
作者姓名:余彬  刘锐  程家迪  范举红  李昌湖  冉坤  曹国华  陈吕军
作者单位:1. 浙江清华长三角研究院生态环境研究所,浙江省水质科学与技术重点实验室,嘉兴314006
2. 浙江清华长三角研究院生态环境研究所,浙江省水质科学与技术重点实验室,嘉兴314006;桐乡市环境保护局,桐乡 314500
3. 桐乡市水务集团有限公司,桐乡,314500
4. 浙江清华长三角研究院生态环境研究所,浙江省水质科学与技术重点实验室,嘉兴314006;清华大学环境学院,北京100084
基金项目:桐乡市科技计划项目(201002029);嘉兴市科技计划项目 (2011AZ1015-1);浙江省科技计划项目(2012C03002-1)
摘    要:针对浙江省某制革园区污水处理厂二级生化出水,开展了处理规模36 t.d-1的臭氧-曝气生物滤池中试研究,考察了不同填料曝气生物滤池沿程高度上污染物的降解规律.结果表明:活性炭曝气生物滤池在沿程1 500 mm处的平均出水COD和色度分别为55.4 mg·L-1和12.6倍,混合填料曝气生物滤池在沿程1 800 mm处的平均出水COD和色度分别为55.6 mg·L-1和9.4倍,出水达到《城镇污水厂污染物排放标准》(GB 18918-2002)中的一级B排放要求.陶粒曝气生物滤池在整个沿程高度上COD和色度变化幅度较小.在沿程高度上活性炭曝气生物滤池和混合填料曝气生物滤池的COD和氨氮在1 200 mm内降幅较大,之后降幅趋缓.3个曝气生物滤池的生物量在沿程900 mm时达到最大,分别为30.69、28.87和15.94 nmol·g-1.

关 键 词:臭氧-曝气生物滤池  制革废水  填料  沿程  污染物  生物量
收稿时间:2012/5/14 0:00:00
修稿时间:2012/10/15 0:00:00

Study on the Pollutants Removal Performance Along the Advanced Treatment in Tannery Wastewater by O3-BAF
Institution:Zhejiang Provincial Key Laboratory of Water Science and Technology, Department of Environmental Technology and Ecology, Yangtze Delta Region Institute of Tsinghua University, Jiaxing 314006, China;Zhejiang Provincial Key Laboratory of Water Science and Technology, Department of Environmental Technology and Ecology, Yangtze Delta Region Institute of Tsinghua University, Jiaxing 314006, China;Zhejiang Provincial Key Laboratory of Water Science and Technology, Department of Environmental Technology and Ecology, Yangtze Delta Region Institute of Tsinghua University, Jiaxing 314006, China;Tongxiang Environmental Protection Agency, Tongxiang 314500, China;Zhejiang Provincial Key Laboratory of Water Science and Technology, Department of Environmental Technology and Ecology, Yangtze Delta Region Institute of Tsinghua University, Jiaxing 314006, China;Tongxiang Water Group Co. Ltd., Tongxiang 314500, China;Tongxiang Water Group Co. Ltd., Tongxiang 314500, China;Tongxiang Water Group Co. Ltd., Tongxiang 314500, China;Zhejiang Provincial Key Laboratory of Water Science and Technology, Department of Environmental Technology and Ecology, Yangtze Delta Region Institute of Tsinghua University, Jiaxing 314006, China;School of Environment, Tsinghua University, Beijing 100084, China
Abstract:A pilot-scale hybrid process of ozone and biological aerated filters (BAF) with the capacity of 36 t·d-1 was applied for advanced treatment of the secondary biologically effluent from a dyeing and tannery park wastewater treatment plant. The pollutants removal performance along the height of different medias BAFs were investigated. The results showed that the average COD and color were 55.4 mg·L-1 and 12.6 times at the height of 1500 mm in activated carbon BAF, and were 55.6 mg·L-1 and 9.4 times at the height of 1800 mm in composite BAF, both of the effluent at each height met the first level B criteria specified in the Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918-2002). Along the height of ceramist BAF, the COD and color were seldom removed. In activated carbon BAF and composite BAF, COD and ammonia nitrogen were both greatly decreased at the height of 1200 mm, then decreased slowly. The biomasses simultaneously reached the maximum at the height of 900 mm in activated carbon, composite and ceramist BAF, with the maxims of 30.69, 28.87 and 15.94 nmol·g-1, respectively.
Keywords:O3-BAF  tannery wastewater  media  along the height  pollutants  biomass
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