工业水处理 ›› 2020, Vol. 40 ›› Issue (4): 67-70. doi: 10.11894/iwt.2019-0427

• 试验研究 • 上一篇    下一篇

单价选择性电渗析处理酸性重金属废水试验研究

李福勤(),焦亚楠,朱云浩,赵桂峰   

  1. 河北工程大学能源与环境工程学院, 河北邯郸 056038
  • 收稿日期:2020-01-04 出版日期:2020-04-20 发布日期:2020-04-21
  • 作者简介:李福勤(1966-),工学博士,教授,硕士生导师,实验室主任。电话:13930086998, E-mail:lifuqin2003@163.com
  • 基金资助:
    河北省重点研发计划项目(19213602D)

Experimental study on treatment of acidic heavy metal wastewater by electrodialysis of monovalent selective

Fuqin Li(),Ya'nan Jiao,Yunhao Zhu,Guifeng Zhao   

  1. College of Energy and Environmental Engineering, Hebei University of Engineering, Handan 056038, China
  • Received:2020-01-04 Online:2020-04-20 Published:2020-04-21

摘要:

采用单价选择性离子交换膜电渗析对污酸中的重金属离子进行分离。考察了电流密度、流量、电压及酸度对H+、Zn2+和Cd2+分离效率的影响。结果表明,污酸酸度(质量分数)为5%,Zn2+和Cd2+初始质量浓度分别为20、5 mg/L,电流密度为25 mA/cm2,淡水室和浓水室流量均为15 L/h,电渗析装置运行168 min时,淡水室中H+透过率为85%,Zn2+和Cd2+泄漏率均为12.86%,重金属离子截留率较高,达到分离污酸中重金属离子的目的。

关键词: 选择性离子交换膜, 电渗析, 酸性重金属废水, 废酸

Abstract:

The separation of heavy metal ions in waste acid is studied by electrodialysis using a monovalent selective ion exchange membrane. The effects of current density, flow rate, voltage and acidity on the separation efficiency of H+, Zn2+ and Cd2+ are investigated, respectively. The results show that when the acidity of waste acid is 5%, the initial concentrations of Zn2+ and Cd2+ are 20 mg/L, 5 mg/L, the current density is 25 mA/cm2, the flow rate of freshwater and concentrated water is 15 L/h, and the electrodialysis device operated for 168 minutes, the H+ transmittance in the freshwater chamber is 85%, and the Zn2+ and Cd2+ leakage rates are 12.86%. The method has a high retention rate of heavy metal ions, which achieves the purpose of separating heavy metal ions in the waste acid.

Key words: selective ion exchange membrane, electrodialysis, acidic heavy metal wastewater, waste acid

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