A kind of waste lithium ion battery recovery method
A technology of lithium-ion batteries and recycling methods, which is applied in the field of recycling waste positive electrode active materials, can solve the problems of secondary pollution of inorganic acid wastewater, affecting the quality of recycled products, and low purity of recycled products, and meets the requirements of lower production equipment , The reaction end point is easy to control, and the effect of reducing the difficulty of extraction and separation
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Embodiment 1
[0079] waste LiNi 0.5 co 0.2 mn 0.3 o 2 The ternary lithium-ion battery is soaked in 5% sulfurous acid solution until the end-of-discharge voltage is 1V, disassembled to obtain the cell, and then mechanically crushed as a whole, and sieved out the debris with a particle size of less than 0.1mm (cell mix material). Gained fragments are uniformly mixed with sodium bisulfate, and the specific parameters are as follows: the positive active material and NaHSO in the battery compound (the weight content of the positive active material is 80%) 4 Mix evenly at a mass ratio of 5:6. Then put the mixed powder into a tube furnace for roasting, the specific parameters are as follows: the roasting temperature is 600° C., and the roasting time is 60 minutes. After the roasting is completed, the obtained samples are subjected to water leaching, and the specific parameters are as follows: leaching temperature 25°C, leaching time 20min, leaching solid-liquid ratio 60g / L; Li leaching soluti...
Embodiment 2
[0084] Compared with Example 1, the main difference is that the mass ratio of the positive electrode active material to sodium bisulfate is controlled to be 5:3. Specifically:
[0085] Adopt the electric core compound material of embodiment 1, the electric core compound material (based on the positive electrode active material weight) and NaHSO 4 Mix evenly at a mass ratio of 5:3. Then put the mixed powder into a tube furnace for roasting, the specific parameters are as follows: the roasting temperature is 600° C., and the roasting time is 60 minutes. After the roasting is completed, the obtained samples are subjected to water leaching, and the specific parameters are as follows: leaching temperature 25°C, leaching time 20min, leaching solid-liquid ratio 60g / L; Li leaching solution and NCM leaching slag (water leaching slag) are obtained.
[0086] Add NaOH to the Li leaching solution, adjust the pH value of the water leaching to 4 to remove iron and aluminum, continue to add...
Embodiment 3
[0090] Compared with Example 2, the difference mainly lies in the use of MnSO 4 As additives, specifically:
[0091] Adopt the cell compound material of embodiment 2, take the positive electrode active material in the cell compound material as a benchmark, combine it with MnSO 4 Mix evenly at a mass ratio of 5:3. Then put the mixed powder into a tube furnace for roasting, the specific parameters are as follows: the roasting temperature is 600° C., and the roasting time is 60 minutes. After the roasting is completed, the obtained samples are subjected to water leaching, and the specific parameters are as follows: leaching temperature 25°C, leaching time 20min, leaching solid-liquid ratio 60g / L; Li leaching solution and NCM leaching slag (water leaching slag) are obtained.
[0092] Add NaOH to the Li leaching solution, adjust the pH value of water leaching to 4 to remove iron and aluminum, continue to add NaOH to the filtrate to adjust the pH value to 10, and then add Na 2 S ...
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