工业水处理 ›› 2015, Vol. 35 ›› Issue (1): 22-25. doi: 10.11894/1005-829x.2015.35(1).022

• 试验研究 • 上一篇    下一篇

离子交换膜电解回收含镍废水中镍的研究

周键1,2, 王三反1,2, 张学敏1,2   

  1. 1. 兰州交通大学环境与市政工程学院, 甘肃兰州 730070;
    2. 寒旱地区水资源综合利用教育部工程中心, 甘肃兰州 730070
  • 收稿日期:2014-11-05 出版日期:2015-01-20 发布日期:2015-03-18
  • 作者简介:周键(1984—),博士,助教。E-mail:zhoujian849200@163.com。
  • 基金资助:

    国家科技支撑计划课题(2012BAF03B06)

Study on ion exchange membrane electrolytic recovery of nickel from nickel-containing wastewater

Zhou Jian1,2, Wang Sanfan1,2, Zhang Xuemin1,2   

  1. 1. School of Environmental and Municipal Engineering, Lanzhou Jiaotong University, Lanzhou 730070, China;
    2. Engineering Research Center for Cold and Arid Regions Water Resource Comprehensive Utilization, Division of Education, Lanzhou 730070, China
  • Received:2014-11-05 Online:2015-01-20 Published:2015-03-18

摘要:

采用双膜三室电解法处理含镍废水,阴极电沉积金属镍,同时可得副产品盐酸,并研究各因素对电解过程的影响规律。结果表明:在电流密度为60 A/m2,pH为4,温度为40℃,Ti/IrTa作为阳极,电解时间为4 h条件下,镍回收率可达82.3%,电流效率高达85.3%,中隔室盐酸浓度为0.5 mol/L,处理后出水经离子交换富集循环使用。

关键词: 含镍废水, 膜电解法, 回收镍, 电流效率

Abstract:

The nickel-containing wastewater has been treated by double-membrane & three-room electrolysis process. Metal nickel can be electrodeposited on the cathode,and by-product,hydrochloric,can be obtained. In addition,the influence rules of factors on the electrolysis process have been studied. When the experimental conditions are as follow:current density is 60 A/m2,pH=4,temperature 40℃,Ti/IrTa as anode,and electrolytic time 4 h,the nickel recovery rate can reach 82.3%,the current efficiency is as high as 85.3%,and the concentration of hydrochloric 0.4 mol/L in the middle compartment,the treated effluent,through ion exchange enrichment,can be used circularly.

Key words: nickel-containing wastewater, membrane electrolysis, nickel recovery, current efficiency

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