Improving Extraction Performance of D2EHPA for ImpuritiesRemoval from Spent Lithium-Ion Batteries Leaching Solution byTPC[4]

被引:16
|
作者
Li, Yunhui [1 ,2 ]
Zeng, Li [1 ,2 ]
Du, Jiawei [1 ,2 ]
Zhang, Guiqing [1 ,2 ]
Cao, Zuoying [1 ,2 ]
Wu, Shengxi [1 ,2 ]
机构
[1] Cent South Univ, Sch Met & Environm, Changsha 410083, Peoples R China
[2] Cent South Univ, Lab Met Separat Sci & Engn, Changsha 410083, Peoples R China
基金
中国国家自然科学基金;
关键词
Spent lithium-ion battery; Solvent extraction; Calixarene; Pyridine; Recovery of valuable metals; SOLVENT-EXTRACTION; NICKEL; METAL; COMPLEXES; MANGANESE; RECOVERY; SYSTEMS; COBALT; ACID; CO;
D O I
10.1021/acssuschemeng.2c00628
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
To reduce reagent consumption, wastewater discharge,and production cost of Mn2+recovery and impurities (Zn2+/Cu2+/Ca2+)removal from an acid leaching solution of spent lithium-ion batteries, amixed extractant (TPC[4]+D2EHPA) was synthesized, and theextraction performances for Mn2+and impurities were systematicallyinvestigated. The synthesis experimental results demonstrated thatTPC[4] can be synthesized in a simple and high yield way with cheapraw materials. Extraction tests indicated that the separation coefficientsof Mn2+,Cu2+, and Zn2+to Ni2+and Co2+by D2EHPA weresignificantly enlarged by the addition of TPC[4], which can mainly beattributed to the enhancement in the differences of binding abilities forcationic complexes with different sizes. Furthermore, the loadingcapacities of Mn2+and impurities (Cu2+,Zn2+) were also enlarged,and the stripping of these cations could easily be achieved with dilute acid. Compared with traditional Mn2+and an impuritiesextraction process with D2EHPA alone, the addition of TPC[4] saved about 10.36% of the saponification alkali (NaOH), 10.36% ofthe washing acid (H2SO4),similar to 20% of the washing water, and more than 4.56% of the organic loss. From both economic andenvironmental perspectives, the mixed solvent of D2EHPA+TPC[4] is an excellent application prospect
引用
收藏
页码:4312 / 4322
页数:11
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