|
| Valuable Metals Recovery from Alkaline Leaching Residue of Copper Anode Slime |
|
Received:July 29, 2016
Revised:August 05, 2016
Accepted:August 08, 2016
Published Online:November 17, 2016
|
| View Full Text View/Add Comment Download reader |
| DOI：doi：10.3969/j.issn.1007-7545.2016.12.012 |
| KeyWord:copper anode slime; alkaline leaching residue; precious metals; enrichment |
| Author | Institution |
| WU Xing-lin |
武汉科技大学 钢铁冶金及资源利用教育部重点实验室 |
| QIN Qing-wei |
武汉科技大学 钢铁冶金及资源利用教育部重点实验室 |
| LIU Zhen-wei |
武汉科技大学 钢铁冶金及资源利用教育部重点实验室 |
| WANG Shao-yu |
武汉科技大学 钢铁冶金及资源利用教育部重点实验室 |
| WANG Shan |
武汉科技大学 钢铁冶金及资源利用教育部重点实验室;湖北大江环保科技股份有限公司;大冶有色金属有限公司稀贵金属厂 |
| LI Wei |
大冶有色金属有限公司稀贵金属厂 |
|
| Hits: 2045 |
| Download times: 2271 |
| Abstract: |
| Alkaline leaching residue of copper anode slime was leached with H2SO4 as leaching agent and NaCl as silver precipitator. The effects of reaction temperature, H2SO4 concentration, NaCl dosage, L/S, and reaction time on leaching of Cu, Te, and Ag were investigated. The results show that leaching rate of Cu, Te, and Ag is 92.82%, 83.69%, and 0.21% respectively under the optimum conditions including H2SO4 concentration of 3 mol/L, NaCl dosage of 6%, L/S=5, reaction temperature of 60 ℃, and leaching time of 1.5 h. Base metals are removed and precious metals are enriched. |
| Close |
|
|
|