Energy Storage Science and Technology ›› 2022, Vol. 11 ›› Issue (12): 3759-3767.doi: 10.19799/j.cnki.2095-4239.2022.0420

• Energy Storage Materials and Devices • Previous Articles     Next Articles

Exploration of mixed positive and negative electrodes of spent lithium iron phosphate batteries

Jian YAO1,2(), Zhaoyang LIU1,2, Hai WANG1,2, Jiadong WANG2, Xuanwen GAO1(), Jianzhong LI1, Zhaomeng LIU1, Yuchun ZHAI1, Wenbin LUO1   

  1. 1.School of Metallurgy, Northeastern University, Shenyang 110000, Liaoning, China
    2.Guangxi Yinyi Advanced Material Company Limited, Yulin 537000, Guangxi, China
  • Received:2022-07-27 Revised:2022-08-08 Online:2022-12-05 Published:2022-12-29
  • Contact: Xuanwen GAO E-mail:2071640@stu.neu.edu.cn;gaoxuanwen@mail.neu.edu.cn

Abstract:

This study explored the selective leaching of valuable metals Li, Cu, and Fe in the mixed positive and negative electrodes of spent LiFePO4 batteries under acidic conditions to simulate the recycling and comprehensive application of spent LiFePO4 batteries in industrial production. The positive and negative electrodes are mechanically crushed and sieved to obtain the mixed powder, which contains high contents of Cu and Al impurities. The carbon and fluorine removal rates are 99.03% and 99.93% after calcination at 700 ℃. When the H+/Li+ molar ratio equals 0.7, the leaching temperature is 90 ℃, the leaching time is 3 h, and the liquid-solid ratio is 3∶1. Additionally, the leaching rates distribution of Li, Fe, Cu, and Al are 91.88%, 0.0024%, 4.71%, 0.11%, respectively, indicating the satisfactory separation of Li. Saturated Na2CO3 successfully recovered the battery-grade lithium carbonate as a precipitant. However, the leaching cinder was calcinated at 450 ℃ to convert Cu into CuO. The metal elements Fe and Cu leaching rates are 0.11% and 92.54%, respectively, under a pH of 1.5, 90 ℃ leaching temperature, 3 h leaching time, and the liquid-solid ratio of 5∶1. Finally, the copper leaching residue was completely dissolved in sulfuric acid. The precipitation rate of ferric phosphate dihydrate reached approximately 95% under adjusting pH to 1.8 by ammonia. The battery-grade ferric phosphate with a purity of 99.48% (weight fraction) was obtained by calcining crystal water.

Key words: spent LiFePO4 battery, mixed recovery of positive and negative electrodes, lithium leaching and recovery, copper leaching and recovery, regenerated iron phosphate

CLC Number: