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基于A^(2)/O工艺污水厂改造与提标工程设计 被引量:3

Design of Sewage Plant Reconstruction and Upgrading Project Based on the A^(2)/O Process
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摘要 南方某污水厂提标扩建工程,一期A^(2)/O好氧区采用MBBR工艺改造并增大缺氧区容积;二期提标采用高效沉淀池+纤维转盘滤池+紫外消毒工艺,强化脱氮除磷及SS去除,并对全厂进行除臭设计。提标扩建后总规模12×10^(4)m^(3)/d,直接运行成本约0.63元/m^(3),出水均值为COD 17.10 mg/L、BOD55.40 mg/L、SS 5.80 mg/L、NH_(4)^(+)-N 0.90 mg/L、TN 5.90 mg/L、TP 0.30 mg/L。均优于《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级A标准,其经验可供其他污水厂借鉴。 Transformation and upgrading engineering design of a sewage treatment plant in South China,the aerobic section of the A^(2)/O tank in phase I was transformed by the MBBR process,and the volume of the anoxic zone was increased.In phase II,the process of A^(2)/O tank+secondary sedimentation tank+high-efficiency sedimentation tank+fiber rotary disc filter+UV disinfection was adopted to strengthen nitrogen and phosphorus removal and SS removal,and the deodorization design of the whole plant was carried out.The total capability after extension was 120000 m^(3)/d.The direct operation cost was about 0.63 yuan/m^(3).The average value of effluent:COD is 17.10 mg/L,BOD5 is 5.40 mg/L,SS is 5.80 mg/L,NH_(4)^(+)-N is 0.90 mg/L,TN is 5.90 mg/L,TP is 0.30 mg/L.All of them were better than the level A criteria of the Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant(GB18918-2002).The experience could be used as a reference for the sewage treatment plants.
作者 姚瑞珍 周国胜 杨新春 陶敏 汪瀚 YAO Ruizhen;ZHOU Guosheng;YANG Xingchun;TAO Ming;WANG Han(School of Environmental Science and Engineering,Hubei Polytechnic University,Huangshi Huli Environmental Protection and Energy Saving Industrial Technology Research Institute Co.,Ltd.,Huangshi 435003,China;Fuzhou Kanggan Water Service Co.,Ltd.,Fuzhou 344100,China)
出处 《水处理技术》 CAS CSCD 北大核心 2024年第2期148-152,共5页 Technology of Water Treatment
基金 湖北省自然科学基金面上项目(2018CFB778) 湖北理工学院重点项目(08yjz08A)。
关键词 A^(2)/O工艺 MBBR工艺 高效沉淀池 纤维转盘滤池 提标改造 A^(2)/O process MBBR process high-efficiency sedimentation fiber rotary disc filter upgrading and reconstruction
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  • 1徐坚,暴瑞玲,刘清,吴娟,鲁金凤.反硝化除磷工艺的影响因素分析[J].当代化工,2020,0(3):729-732. 被引量:4
  • 2王攀,彭党聪.预缺氧池配水比对Johannesburg工艺脱氮除磷效果的影响[J].环境工程学报,2015,9(4):1645-1650. 被引量:2
  • 3王学江,夏四清,陈玲,赵建夫.DO对MBBR同步硝化反硝化生物脱氮影响研究[J].同济大学学报(自然科学版),2006,34(4):514-517. 被引量:62
  • 4刘建广,付昆明,杨义飞,张维健.不同电子受体对反硝化除磷菌缺氧吸磷的影响[J].环境科学,2007,28(7):1472-1476. 被引量:40
  • 5Robertson L A, Kuenen J G. Aerobic Denitrification: a Controversy Revived[J]. Arch Microbiol, 1984, 139(5): 351-354.
  • 6Klangduen Pochana, Jurg Keller. Study of Factors Affecting Simultaneous Nitrification and Denitrification (SND)[J]. Wat Sci Tech, 1999, 39(6): 61-68.
  • 7Robertson L A. Nitrogen Removal from Water and Waste[A]. In:Microbial Control of Pollution [C]. Cambridge: Cambridge University Press, 1992. 227-267.
  • 8A B Gupta. Thiosphaeera Pantotropha a Sulphur Bacterium Capable of Simultaneous Heterotrophic Nitrification and Aerobic Denitrification[J]. Enzyme and Microbile Technology, 1997, 21(8): 589-595.
  • 9L A Robertson, ED W J VAN Niel, ROB A M Torremans, et al. Simultaneous Nitrification and Denitrification in Aerobic Chemostat Cultures of Thiosphaeera Pantotropha[J]. Applied and Environmental Microbiology, 1988, 54(11): 2812-2818.
  • 10Mike S M Jetten, Susanne logemann, Gerard Muyzer, et al.Novel Principle in the Microbial Conversion of Nitrogen Compounds [J]. Antonie van Leeuwenhoek, 1997, 71 (1 -2):75-93.

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