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Recovery of Co(II) and Ni(II) from hydrochloric acid solution of alloy scrap
其他题名Recovery of Co(II) and Ni(II) from hydrochloric acid solution of alloy scrap
Shen Yongfeng1; Xue Wenying3; Niu Wenyong3
2008
发表期刊TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA
ISSN1003-6326
卷号18期号:5页码:1262-1268
摘要A hydrometallurgical process was developed for recovery of nickel and cobalt from the hydrochloric acid leaching solution of alloy scraps. The process consists of five major unit operations: 1) leaching with 6 mol/L hydrochloric acid under the L/S ratio of 10:1 at 95 degrees C for 3 h; 2) copper replacement by iron scraps under pH value of 2.0 at 80 degrees C, and stirring for 1 h; 3) removal of iron and chromium by chemical precipitation: iron removal under pH value of 2.0 at 90 degrees C by dropwise addition of sodium chlorate and 18% sodium carbonate solution, then chromium removal under pH value of 4.0 at 70 degrees C by addition of nickel carbonate solution, stirred by air flow for 2 h 4) selective separation of cobalt from nickel by extraction using 30% trialkyl amine+50% kerosene (volume fraction) and tri-n-butylphosphate (TBP) as a phase modifier with the O/A ratio of 2:1, and stripping of cobalt with 0.01 mol/L HCl; 5) crystallization of nickel chloride and eletrodeposition of cobalt. It is found that the nickel recovery of 95% and the cobalt recovery of approximately 60% with purity over 99.9% are obtained by this process.
其他摘要A hydrometallurgical process was developed for recovery of nickel and cobalt from the hydrochloric acid leaching solution of alloy scraps. The process consists of five major unit operations: 1) leaching with 6 mol/L hydrochloric acid under the L/S ratio of 10:1 at 95 °C for 3 h; 2) copper replacement by iron scraps under pH value of 2.0 at 80 °C, and stirring for 1 h; 3) removal of iron and chromium by chemical precipitation: iron removal under pH value of 2.0 at 90 °C by dropwise addition of sodium chlorate and 18% sodium carbonate solution, then chromium removal under pH value of 4.0 at 70 °C by addition of nickel carbonate solution, stirred by air flow for 2 h; 4) selective separation of cobalt from nickel by extraction using 30% trialkyl amine+50% kerosene (volume fraction) and tri-n-butylphosphate (TBP) as a phase modifier with the O/A ratio of 2:1, and stripping of cobalt with 0.01 mol/L HCl; 5) crystallization of nickel chloride and electrodeposition of cobalt. It is found that the nickel recovery of 95% and the cobalt recovery of approximately 60% with purity over 99.9% are obtained by this process.
关键词LITHIUM-ION BATTERIES NI-CD BATTERIES SOLVENT-EXTRACTION SULFATE-SOLUTIONS SULFURIC-ACID NICKEL COBALT SEPARATION MIXTURES COPPER alloy scrap nickel cobalt recovery trialkyl amine
收录类别CSCD
语种英语
资助项目[National Natural Science Foundation of China]
CSCD记录号CSCD:3371042
引用统计
被引频次:11[CSCD]   [CSCD记录]
文献类型期刊论文
条目标识符http://ir.imr.ac.cn/handle/321006/155863
专题中国科学院金属研究所
作者单位1.上海市地震局
2.中国科学院金属研究所
3.东北大学
推荐引用方式
GB/T 7714
Shen Yongfeng,Xue Wenying,Niu Wenyong. Recovery of Co(II) and Ni(II) from hydrochloric acid solution of alloy scrap[J]. TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA,2008,18(5):1262-1268.
APA Shen Yongfeng,Xue Wenying,&Niu Wenyong.(2008).Recovery of Co(II) and Ni(II) from hydrochloric acid solution of alloy scrap.TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA,18(5),1262-1268.
MLA Shen Yongfeng,et al."Recovery of Co(II) and Ni(II) from hydrochloric acid solution of alloy scrap".TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA 18.5(2008):1262-1268.
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