<p>Nowadays, the recycling of spent lithium-ion batteries is a key concern in the energy field. Among them, for the purification of Li-containing mother liquor, the targeted multi-means coupling impurity removal methods are mostly employed, which however, inevitably lead to a Li loss of 3–5% and high costs. In this study, a multi-stage hydrolysis method, combining the residual P and Al, Mg, Cu, Zn, Ni, Fe, forming hydroxide-phosphate co-precipitation for the synergistic impurity separation, was adopted. Thermodynamic calculations show that Li<sup>+</sup> and Mg<sup>2+</sup> are insensitive to pH when pH &lt; 10, and Al, Cu, Zn, Ni, Fe behave similarly in nature. The impurities should be precipitated as: Fe<sup>3+</sup> &gt; Al<sup>3+</sup> &gt; Cu<sup>2+</sup> &gt; Ni<sup>2+</sup> &gt; Zn<sup>2+</sup> &gt; Mg<sup>2+</sup>, with phosphate precipitating first, followed by converting into hydroxide as pH rising. Actual results showed that the order was P &gt; Fe &amp; Al &amp; Cu &amp; Ni &amp; Zn &gt; Mg, and the process was divided into three steps, with separation points at pH = 2.37, 8.66, and 11.00, respectively. All the impurity removal efficiencies were close to 100%, the loss of Li was 1.74%. The optimal conditions for Li<sub>2</sub>CO<sub>3</sub> precipitation were determined: an Na<sub>2</sub>CO<sub>3</sub> addition of 1.5 times the theoretical amount, a temperature of 90&#xa0;°C, a reaction time of 4&#xa0;h, and a one-time addition of dosing method. Li precipitation efficiency reaches 90.10%, with a 99.95% purity. The results effectively reduced Li losses and provided a practically feasible basis for the industrial purification of Li-containing mother liquor.</p>

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Spent Lithium-Ion Battery Recycling: Multi-stage Synergistic Deep Removal of Impurities and Lithium Extraction

  • Wen-bo Lou,
  • Dong-yan Liu,
  • Yun Wang,
  • Da Zhao,
  • Zi-cheng Sun,
  • Yi Zou,
  • Sheng-yan Wang,
  • Quan-guo Cheng,
  • Jian-zhong Li,
  • Hong-hui Liu

摘要

Nowadays, the recycling of spent lithium-ion batteries is a key concern in the energy field. Among them, for the purification of Li-containing mother liquor, the targeted multi-means coupling impurity removal methods are mostly employed, which however, inevitably lead to a Li loss of 3–5% and high costs. In this study, a multi-stage hydrolysis method, combining the residual P and Al, Mg, Cu, Zn, Ni, Fe, forming hydroxide-phosphate co-precipitation for the synergistic impurity separation, was adopted. Thermodynamic calculations show that Li+ and Mg2+ are insensitive to pH when pH < 10, and Al, Cu, Zn, Ni, Fe behave similarly in nature. The impurities should be precipitated as: Fe3+ > Al3+ > Cu2+ > Ni2+ > Zn2+ > Mg2+, with phosphate precipitating first, followed by converting into hydroxide as pH rising. Actual results showed that the order was P > Fe & Al & Cu & Ni & Zn > Mg, and the process was divided into three steps, with separation points at pH = 2.37, 8.66, and 11.00, respectively. All the impurity removal efficiencies were close to 100%, the loss of Li was 1.74%. The optimal conditions for Li2CO3 precipitation were determined: an Na2CO3 addition of 1.5 times the theoretical amount, a temperature of 90 °C, a reaction time of 4 h, and a one-time addition of dosing method. Li precipitation efficiency reaches 90.10%, with a 99.95% purity. The results effectively reduced Li losses and provided a practically feasible basis for the industrial purification of Li-containing mother liquor.