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《采用溶剂萃取从废旧锂离子电池中回收有价金属.》.pdf

发布:2016-01-05约字共15页下载文档
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Recovery of metal values from spent lithium-ion battery leach solutions with solvent extraction Guochun Yan Contents What Why How 2 What  Solvent extraction  Spent lithium-ion battery 3 Why  Global lithium demand  Environment protection  More strict legislation  Battery economic 4 How Dismantling Leaching Solvent extraction 5 Leaching  Agent:H SO +H O 2 4 2 2  Codition:75 0C,1h,3OOr/min  Extraction ratio:Co,Li95% Typical composition of leach solution(g/L) Co2+ Li+ Fe3+ Al3+ Ni2+ Cu2+ 16.9 3.8 0.6 0.7 0.15 0.4 6 Extracting  Extractant:lonquest 801+acogra M5640 for (Al,Fe,Cu) Cyanex272 for (Co)  Diulent:Shellsol D70 The metal pH0.5 values in the extract system Metal Fe Al Cu Co Li Ni pH0.5 0.5 3.15 2.00 N/A N/A N/A 7 Extracting(1) Extraction order FeCuAlCo,Ni,Li 0 Metal pH isotherms at an O:A ratio of 1:2 and 22 C 8 Extracting(1) Metal
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