期刊文献+

HCl-CuCl_2-NaClO湿法浸取手机元器件中的钯、金 被引量:2

Extraction of Pd,Au from Phone components in HCl-Cu Cl_2-Na Cl O solutions
下载PDF
导出
摘要 通过HCl-Cu Cl2-Na Cl O湿法浸出体系对手机元器件中金属钯(Pd)、金(Au)进行浸出实验,研究不同因素对于Pd、Au浸出率的影响.结果显示,在2mol/L HCl、体积分数5%Na Cl O、0.075mol/L Cu Cl_2、固液比1%,反应温度60℃条件下,2h后Pd、Au浸出率均可达85%;结果表明,Cu^(2+)、Cl-、温度对于Pd的浸出率起很大作用,Na Cl O的加入可加快Pd浸出反应达到平衡速率;Na Cl O、温度对于Au的浸出率起关键作用,HCl、Cu^(2+)的加入可促进Au的浸出.因此,HCl-Cu Cl_2-Na Cl O湿法浸出体系对于Pd、Au具有良好的浸出效果. A novel hydrometallurgical process for recovery of palladium and gold from phone components inHCl-CuCl2-NaClO leaching system was offered,different factors of Pd,Au leaching process were investigated.Theresults of experiment indicated that,on the condition of2mol/L HCl,5%NaClO,0.075mol/L CuCl2at333K for2h with asolid/liquid ratio of1/100,over85%of Pd and Au was leached.Cu2+,Cl-,the temperature for the Pd leaching rates playeda significant role.NaClO was added to solutions could accelerate the Pd leaching reaction rates;NaClO,the temperaturefor the Au leaching rates had a significant influence.The additions of HCl,Cu2+to promotes Au leaching.Therefore,HCl-CuCl2-NaClO leaching system for Pd,Au leaching have a positive effect.
作者 丁江铃 张小平 朱亚茹 张天雨 刘竞辉 ZHANG Xiao-ping;ZHU Ya-ru;ZHANG Tian-yu;LIU Jing-hui;DING Jiang-ling(School of Environment and Energy, South China University of Technology, Guangzhou 510006, China;Key Laboratory of Pollution Control and Ecosystem Restoration Industry Clusters, Ministry of Education, Guangzhou 510006, China;Guangdong Environmental Protection Key Laboratory of Solid Waste Treatment and Recycling, Guangzhou 510006, China)
出处 《中国环境科学》 EI CAS CSCD 北大核心 2016年第12期3711-3716,共6页 China Environmental Science
基金 国家自然科学基金(21377041) 广东省科技计划项目(2013B021300022) 亚热带建筑科学基金会国家重点实验室(2013KB28)
关键词 电子废弃物 铜-氯体系 湿法浸出 手机 waste electrical and electronic equipment gold palladium cupric-chloride leaching hydrometallugry mobile phone
  • 相关文献

参考文献2

二级参考文献48

  • 1王治科,陈东辉,陈亮.热力学分析氯化浸金体系规律[J].稀有金属,2006,30(5):703-706. 被引量:11
  • 2Aylmore M G. Alternative lixiviants to cyanide for leaching gold ores [ J]. Developments in Mineral Processing, 2005, 15: 501.
  • 3Senanayake G. Gold leaching in non-cyanide lixiviant systems: critical issues on fundamentals and applications [ J ]. Minerals Engineering, 2004, 17 : 785.
  • 4Gavin Hilson, Monhemius A J. Ahernatives to cyanide in the gold mining industry: what prospects for the future [ J ]. Journal of Cleaner Production, 2006, 14 : 1158.
  • 5Baghalha M. Leaching of an oxide gold ore with chloride and hypochlorite solutions [ J ]. International Journal of Mineral Process, 2007, 82: 178.
  • 6Puvvada G V K, Murthy D S R. Selective precious metals leaching from a chaleopyrite concentrate using chloride/hypochlorite media [ J]. Hydrometallurgy, 2000, 58 : 185.
  • 7Kwang Soo Nam, Byoung Hi Jung, Jeon Woong An, Tae Jun Ha, Tam Tran, Myong Jun Kim. Use of chloride-hypochlorite leachants to recover gold from tailing [ J ]. International Journal of Mineral Process, 2008, 86: 131.
  • 8John Marsden, Iain Hous. The Chemistry of Gold Extraction [M]. Littleton: SME, 2006. 271.
  • 9Jeffrey M I, Breuer P L, Choo W L A kinetic study that compares the leaching of gold in the Cyanide, Thiosulfate, and Chloride systems [ J ]. Metallurgical and Materials Transactions B, 2001, 32B : 979.
  • 10Vinals J, Nunez C, Herreres O. Kinetics of the aqueous chlorination of gold in suspended particles [ J]. Hydrometallurgy, 1995,38 : 125.

共引文献40

同被引文献21

引证文献2

二级引证文献6

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部