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
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ISSN | 1003-6326 |
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 | |
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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