INDUSTRIAL WATER TREATMENT ›› 2016, Vol. 36 ›› Issue (5): 82-86. doi: 10.11894/1005-829x.2016.36(5).082

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Research on the advanced treatment of tail water in wastewater treatment plants by two-stage oyster shells fix-bed-membrane bioreactors (MBR) process

Liu Shinian1,2, Chen Junfeng1, Yan Jia1, Li Xin2, Lü Wangyan2, Hu Yongyou1, Hong Tian1   

  1. 1. The Key Lab of Pollution Control and Ecosystem Restoration in Industry Clusters, Ministry of Education, School of Environment and Energy, South China University of Technology, Guangzhou 510006, China;
    2. Electric Power Research Institute of Guangdong Power Grid Co., Ltd., Guangzhou 510080, China
  • Received:2016-02-14 Online:2016-05-20 Published:2016-06-24

二级牡蛎壳固定床-MBR工艺深度处理尾水研究

刘世念1,2, 陈峻峰1, 阎佳1, 李欣2, 吕旺燕2, 胡勇有1, 洪添1   

  1. 1. 华南理工大学环境与能源学院, 工业聚集区污染控制与生态修复教育部重点实验室, 广东广州 510006;
    2. 广东电网有限责任公司电力科学研究院, 广东广州 510080
  • 通讯作者: 胡勇有,教授,博士生导师。E-mail:ppyyhu@scut.edu.cn。 E-mail:ppyyhu@scut.edu.cn
  • 作者简介:刘世念(1971-),高级工程师。E-mail:gz_liusn@163.com。
  • 基金资助:

    污(废)水资源化及回用集成技术研究项目(K-GD2013-0501002-001)

Abstract:

By utilizing the strong oxidation of ozone,degradation of microbes and strong interception of MBR,the technological flow of the two-stage oyster shells fix-bed OOFR-AOFB-MBR system is established for the advanced treatment of tail water in wastewater treatment plants.The results from a 90 d bench scale experiment show that this process can effectively remove C,N,P and suspended solids from tail water.The boundary dosage of ozone is 40-110 mg/L,and when the optimum ozone dosage concentration in ozone oyster shells fix-bed reactor is about 90 mg/L.the removing rates of system COD,NH4+-N and TP are 83%,99% and 65%,respectively,the average effluent COD,NH4+-N and TP are 6,0.1,0.14 mg/L,respectively,the turbidity is lower than 0.1 NTU,and pH is 7.4-7.8,meeting completely the requirements for reverse osmosis to treat influent.

Key words: municipal tail water, ozone oyster shells fix-bed, aeration oyster shells fix-bed, advanced treatment

摘要:

利用臭氧的强氧化、微生物降解以及MBR的强截留作用,构建了二级牡蛎壳固定床,即OOFR(臭氧-牡蛎壳固定床)-AOFB(曝气-牡蛎壳生物固定床)-MBR深度处理污水厂尾水工艺流程。为期90 d的小试结果表明,该工艺可高效地去除尾水中的C、N、P以及悬浮物。臭氧边界投加量为40~110 mg/L,在臭氧最佳投加量90 mg/L下,系统的COD、NH4+-N、TP的平均去除率分别达83%、99%、65%,平均出水COD、NH4+-N、TP分别为6、0.1、0.14 mg/L,浊度低于0.1 NTU,pH为7.4~7.8,完全满足反渗透处理进水的要求。

关键词: 市政尾水, 臭氧-牡蛎壳固定床, 曝气-牡蛎壳生物固定床, 深度处理

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