INDUSTRIAL WATER TREATMENT ›› 2011, Vol. 31 ›› Issue (9): 86-87. doi: 10.11894/1005-829x.2011.31(9).86

Previous Articles     Next Articles

Engineering example of printing and dyeing wastewater treatment

Zhan Xu1, Chen Yanhong1, Li Dacheng2, Tu Kai1, Shao Shuai1   

  1. 1. School of Environment and Civil Engineering, Jiangnan University, Wuxi 214112, China;
    2. Wuxi Municipal Design Institute Co., Ltd., Wuxi 214205, China
  • Received:2011-07-16 Revised:2011-07-16 Published:2011-09-29

印染废水处理工程实例

詹旭1, 陈艳红1, 李大成2, 涂凯1, 邵帅1   

  1. 1. 江南大学环境与土木工程学院, 江苏无锡 214112;
    2. 无锡市政设计研究院有限公司, 江苏无锡 214205
  • 作者简介:詹旭(1981- ),2008 年毕业于东南大学, 博士, 副教授。E-mail:zhanxu_010@163.com。

Abstract:

The combined dynamic microelectrolysis/hydrolysis acidification/aerobic biochemistry process has been used as the main work in the treatment of printing and dyeing wastewater. The results show that when the influent CODCr is 2 160.0 mg/L,BOD5 613.0 mg/L,SS 310.0 mg/L,chroma 560.0,and NH3-N 38.0 mg/L,the treated effluent CODCr reaches 64.5 mg/L,BOD5 18.6 mg/L,SS 11.8 mg/L,chroma 35.1,and NH3-N 5.1 mg/L,achieving the first class of Discharge Standard of Water Pollutants for Dyeing and Finishing of Textile Industry(GB 4287-1992).

Key words: printing and dyeing wastewater, microelectrolysis;hydrolysis, aerobic

摘要:

采用动态微电解/水解酸化/好氧生化法为主体的工艺处理印染废水。工程运行结果表明:进水CODCr为2 160.0 mg/L,BOD5为613.0 mg/L,SS为310.0 mg/L,色度为560.0倍,氨氮为38.0 mg/L时处理后出水的CODCr为64.5 mg/L,BOD5为18.6 mg/L,SS为11.8 mg/L,色度为35.1倍,氨氮为5.1 mg/L,可达到GB 4287-1992《纺织染整工业水污染物排放标准》的一级标准要求。

关键词: 印染废水, 微电解, 水解, 好氧

CLC Number: