期刊文献+

Electrodeposition conditions of metallic nickel in electrolytic membrane reactor 被引量:10

离子交换膜电解槽中电沉积金属镍(英文)
在线阅读 下载PDF
导出
摘要 The process parameters were optimized for the eleetrodeposition of nickel in an electrolytic membrane reactor. Nickel(Ⅱ) and boric acid concentrations, pH and temperature were varied to evaluate the changes in current efficiency and specific energy consumption of nickel electrodeposition. The catholyte was aqueous nickel(Ⅱ) sulfate and boric acid, and the anolyte was sulfuric acid solution. An anionic membrane separated the anolyte from the catholyte while maintained a conductive path between the two compartments. The results indicated that the cathode current efficiency increased with the increase of nickel concentration, pH and boric acid concentration, and decreased with the increase of current density and stirring rate. A maximum current efficiency of 97.15% was obtained under the optimized conditions of electrolyte composition of 40 g/L Ni and 40 g/L boric acid at temperature of 42 ℃ and pH of 6 with a cathode current density of 300 A/m2. 对离子交换膜电解槽中电沉积金属镍的条件进行优化。研究镍(II)及硼酸浓度、pH及温度对电沉积镍的电流效率和能耗的影响。电解槽阴极液为含硼酸的硫酸镍溶液,阳极液为硫酸溶液。采用阴离子交换膜将阴、阳极室隔开,同时维持极室间的导电性。结果表明:阴极电流效率随镍和硼酸浓度以及pH值的增加而提高,随电流密度和搅拌速率的增大而降低。得到的优化电解条件为:Ni40g/L、硼酸40g/L、温度42oC、pH6、阴极电流密度300A/m2。在该条件下的电流效率为97.15%。
出处 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2012年第2期467-475,共9页 中国有色金属学报(英文版)
关键词 NICKEL eleetrodeposition anion-exchange membrane electrolytic membrane reactor 电沉积 阴离子交换膜 膜电解槽
  • 相关文献

参考文献34

  • 1ANTHONY M T, FLETT D S. Nickel processing technology: A review [J]. Minerals Industry International,1997,1: 26-42.
  • 2SUDOL S. The thunder from down under: Everything you wanted to know about laterites but were afraid to ask [J]. Canadian Mining Journal,2005,126(5): 8-12.
  • 3MOSKALYK R R, ALFANTAZI A M. Nickel sulphide smelting and electrorefining practice: A review [J]. Mineral Processing and Extractive Metallurgy Review,2002,23(3/4): 141-180.
  • 4HOLM M, O'KEEFE T J. Electrolyte parameter effects in the electrowinning of nickel from sulfate electrolytes [J]. Minerals Engineering,2000,13(2): 193-204.
  • 5TILAK B V, GENDRON A S, MOSOIU M A. Borate buffer equilibria in nickel refining electrolytes [J]. Journal of Applied Electrochemistry,1977,7(6): 495-500.
  • 6MUIR D M, HO E. Process review and electrochemistry of nickel sulphides and nickel mattes in acidic sulphate and chloride media [J]. Mineral Processing and Extractive Metallurgy,2006,115(2): 57-65.
  • 7LUPI C, PASQUALI M, DELLERA A. Studies concerning nickel electrowinning from acidic and alkaline electrolytes [J]. Minerals Engineering,2006. 19(12): 1246-1250.
  • 8PALMER C M,JOHNSON G D. The Activox- process: Growingsignificance in the nickel industry [J]. JOM,2005,57(7): 40-47.
  • 9REN Hong-jiu, WANG Li-chuan. A handbook for extractive metallurgy of nonferrous metals [M]. Beijing: Metallurgical Industry Press,2000: 664-665. (in Chinese).
  • 10JI J X. Fundamental aspects of nickel electrowinning from chloride electrolytes [D]. Canada: The University of British Columbia,1994: 15-20.

同被引文献155

引证文献10

二级引证文献41

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