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从电镀污泥中回收镍、铜和铬的工艺研究

郭学益, 石文堂, 李栋, 田庆华

郭学益, 石文堂, 李栋, 田庆华. 从电镀污泥中回收镍、铜和铬的工艺研究[J]. 工程科学学报, 2011, 33(3): 328-333. DOI: 10.13374/j.issn1001-053x.2011.03.006
引用本文: 郭学益, 石文堂, 李栋, 田庆华. 从电镀污泥中回收镍、铜和铬的工艺研究[J]. 工程科学学报, 2011, 33(3): 328-333. DOI: 10.13374/j.issn1001-053x.2011.03.006
GUO Xue-yi, SHI Wen-tang, LI Dong, TIAN Qing-hua. Recycling process of nickel,copper and chromium from the electroplating sludge[J]. Chinese Journal of Engineering, 2011, 33(3): 328-333. DOI: 10.13374/j.issn1001-053x.2011.03.006
Citation: GUO Xue-yi, SHI Wen-tang, LI Dong, TIAN Qing-hua. Recycling process of nickel,copper and chromium from the electroplating sludge[J]. Chinese Journal of Engineering, 2011, 33(3): 328-333. DOI: 10.13374/j.issn1001-053x.2011.03.006

从电镀污泥中回收镍、铜和铬的工艺研究

详细信息
    通信作者:

    郭学益,E-mail:xyguo@mail.csu.edu.cn

  • 分类号: X781.1

Recycling process of nickel,copper and chromium from the electroplating sludge

  • 摘要: 采用硫酸浸出-硫化沉铜-两段中和除铬-碳酸镍富集工艺,从电镀污泥中综合回收铜、铬和镍.考察了各工序过程中的影响因素,获得了最佳工艺条件:酸浸过程中反应时间为0.5 h,反应温度为50℃,硫酸加入量为理论量的0.8倍;沉铜过程中,沉铜剂加入量为理论量的1.2倍,反应时间和反应温度分别为1 h和85℃;采用两段除铬工序有效降低了沉淀过程中的镍损失.整个工艺中,铜、铬和镍的回收率分别达到98%、99%和94%以上.
    Abstract: The electroplating sludge was treated for the comprehensive recovery of copper, chromium and nickel with procedures including sulfuric acid leaching, copper precipitation, chromium removal by two-stage neutralization, and nickel carbonate concentrating. Various processing factors were studied and the optimum conditions were obtained as follows:0.5 h, 50℃, and 0. 8 times of stoichiometric sulfuric acid addition for sulfuric acid leaching; 1 h, 85℃, and 1.2 times of stoichiometric copper precipitator addition for copper precipitation; the two-stage chromium removal method decreases nickel loss in the precipitation process. More than 98% of copper, 99% of chromium and 94% of nickel originally contained in the sludge were successfully recovered by using this process.
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出版历程
  • 收稿日期:  2010-02-04
  • 网络出版日期:  2021-07-29
  • 刊出日期:  2011-03-24

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