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Valorization of waste NiMH battery through recovery of critical rare earth metal: A simple recycling process for the circular economy

机译:通过回收关键的稀土金属来实现NiMH废电池的回收利用:循环经济的简单回收过程

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The process flowsheet consists of three main circuits, i.e., metal extraction by acid leaching, critical rare earth metal (REM) recovery from leach liquor and pure Co/Ni recovery by solvent extraction. Quantitative metal extraction using 1 M H_2SO_4, pulp density of 25 g/L at 90 ℃ from waste NiMH battery was achieved. From leach liquor using 10 M NaOH, at pH 1.8, more than 99% REM was precipitated out and isolated through calcination at 600 ℃. Undesired metals like Mn, Al, Zn, and Fe were scrubbed out from the leach liquor using 0. 7 M D2EPHA at the equilibrium pH of 2.30. From the scrubbed raffinate Co and Ni was separated using 0.5 M Cyanex 272 at pH 4.70 through solvent extraction. At pH 4.70 Co was completely extracted from solution leaving Ni in solution, which can be recovered completely. From Co loaded Cyanex 272, the Co was stripped by 1 M H_2SO_4 and regenerated Cyanex 272 can be reused and close the loop. Similarly, the undesired metal loaded D2EPHA can be regenerated and reused and close the loop. As the process is close-loop process recovers critical REMs, Co, and Ni, the valorization process effi-ciently addresses the circular economy and recycling challenges associated with waste NiMH battery.
机译:该工艺流程包括三个主要流程,即通过酸浸进行金属萃取,从浸出液中回收关键稀土金属(REM)和通过溶剂萃取进行纯Co / Ni回收。使用1 M H_2SO_4定量提取金属,废镍氢电池在90℃下纸浆密度为25 g / L。在pH值为1.8的条件下,使用10 M NaOH从浸出液中沉淀出超过99%的REM,并通过在600℃下煅烧进行分离。在平衡pH为2.30的情况下,使用0. 7 M D2EPHA从浸出液中洗出了不需要的金属,如Mn,Al,Zn和Fe。使用0.5 M Cyanex 272在pH 4.70下通过溶剂萃取从洗涤后的残液中分离出Co和Ni。在pH值为4.70时,从溶液中完全萃取出Co,溶液中留有Ni,可以完全回收。从含钴的Cyanex 272中,用1 M H_2SO_4脱除Co,然后可以重新使用再生的Cyanex 272并关闭回路。同样,不需要的金属负载D2EPHA可以重新生成并重新使用并关闭循环。由于该过程是闭环过程,可回收关键的REM,Co和Ni,因此增值过程可有效应对循环经济和镍氢废电池带来的循环利用挑战。

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