华南理工大学学报(自然科学版) ›› 2006, Vol. 34 ›› Issue (12): 10-14.

• 环境科学与技术 • 上一篇    下一篇

O3-BAC给水深度处理工艺的优化运行

陆少鸣1 王宁1 杨立2   

  1. 1. 华南理工大学 环境科学与工程学院, 广东 广州 510640; 2. 华南理工大学 建筑设计研究院, 广东 广州 510640
  • 收稿日期:2005-12-20 出版日期:2006-12-25 发布日期:2006-12-25
  • 通信作者: 陆少鸣(1958-) ,男,副教授,主要从事环境工程和给水排水工程技术研究. E-mail:Lushaom@163. com
  • 作者简介:陆少鸣(1958-) ,男,副教授,主要从事环境工程和给水排水工程技术研究.
  • 基金资助:

    建设部科技计划资助项目(04222064)

Operation Optimization of O3-BAC Advanced Treatment Process for Drinking Water

Lu Shao-mingWang NingYang Li2   

  1. 1. School of Environmental Science and Engineering, South China Univ. of Tech. , Guangzhou 510640, Guangdong, China;2. Academe ofArchitecture Design, South China Univ. of Tech. , Guangzhou 510640, Guangdong, China
  • Received:2005-12-20 Online:2006-12-25 Published:2006-12-25
  • Contact: 陆少鸣(1958-) ,男,副教授,主要从事环境工程和给水排水工程技术研究. E-mail:Lushaom@163. com
  • About author:陆少鸣(1958-) ,男,副教授,主要从事环境工程和给水排水工程技术研究.
  • Supported by:

    建设部科技计划资助项目(04222064)

摘要: 通过工艺Ⅰ (预臭氧+常规处理+后臭氧+生物炭滤) 和工艺Ⅱ (预臭氧+常规处理+生物炭滤)的对比试验,对属于Ⅱ~Ⅲ类地表水的广州市东江水源进行臭氧- 生物活性炭(O3-BAC)深度净水中试,研究了污染物的去除规律,并对照南洲水厂的实际运行效果,提出了依据原水不同水质状况优化运行的建议. 中试结果表明,当水源CODMn低于3. 0mg/L 及氨氮含量低于1. 0mg/L 时,可按工艺Ⅱ方式运行; 当水源CODMn高于3. 5mg/L或氨氮含量高于1. 5mg/L时,需要按工艺Ⅰ方式运行,以确保出水达到标准. 南洲水厂运行结果也表明,可根据原水水质分别按照工艺Ⅰ或工艺Ⅱ方式优化运行.

关键词: 原水, 水质, 臭氧, 生物活性炭, 深度处理, 运行优化

Abstract:

A pilot-scale experiment of O3-biological activated carbon (O3-BAC) advanced treatment process was carried out for the surface water at levels Ⅱ~Ⅲ in the Dongjiang River, Guangzhou. The removal rules of the con-tamination in the water were then investigated. In the experiment, two processes, namely Process I-pre-ozone +conventional treatment p rocess +O3 +BAC and Process Ⅱ-p re-ozone + conventional treatment p rocess +BAC were adop ted to perform a contrast test. The experimental results were finally compared with the practical data of the Nanzhou Drinking-Water Treatment Plant. Some suggestions for the optimization of O3-BAC process were made in accordance with the quality of the raw water. The results of the p ilot2scale experiment show that, in order to ensure the drinking-water quality, Process Ⅱ should be adop ted when the raw water is of a CODMn of no more than 3. 0mg/L and a NH3-N content of no more than 1. 0mg/L, and that ProcessⅠshould be adopted when the raw wa-ter is of a CODMn ofmore than 3. 5mg/L or a NH3-N content ofmore than 1. 5mg/L. The p ractical operation results of the Nanzhou Drinking2Water Treatment Plant also reveal that Processes Ⅰand Ⅱ can be alternately adop ted in accordance with the quality of the raw water.

Key words: raw water, water quality, ozone, biological activated carbon, advanced treatment, operation optimiza