Method for recovering active metals from lithium secondary battery
US-2021115532-A1 · Apr 22, 2021 · US
US2024154197A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024154197-A1 |
| Application number | US-202118333643-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 15, 2021 |
| Priority date | Dec 22, 2020 |
| Publication date | May 9, 2024 |
| Grant date | — |
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In a method for recovering an active metal of a lithium secondary battery, positive electrode active material particles including a lithium-transition metal oxide is prepared. The positive active material particles are treated by reduction. The reduction-treated positive active particles are subjected to ultrasonic dispersion and hydration. The hydrated transition metal slurry is recovered. The recovery rate of lithium and transition metal can be increased by disaggregation through ultrasonic dispersion.
Opening claim text (preview).
What is claimed is: 1 . A method for recovering an active metal of a lithium secondary battery, comprising: preparing cathode active material particles containing a lithium-transition metal oxide; performing a reduction treatment of the cathode active material particles; performing an ultrasonic wave dispersing hydration of the reduced cathode active material particles; and recovering a hydrated transition metal slurry. 2 . The method of claim 1 , wherein the reduction treatment comprises forming lithium precursor particles, transition metal oxide particles and transition metal particles from the cathode active material particles. 3 . The method of claim 2 , wherein aggregates of the lithium precursor particles, the transition metal oxide particles and the transition metal particles are formed in the reduction treatment. 4 . The method of claim 3 , wherein the ultrasonic wave dispersing hydration comprises decomposing the aggregates. 5 . The method of claim 4 , wherein the aggregates are decomposed into particles having a particle size of 300 μm or less through the ultrasonic wave dispersing hydration. 6 . The method of claim 1 , wherein the ultrasonic wave dispersing hydration comprises a solid-liquid two-phase process. 7 . The method of claim 1 , wherein the ultrasonic wave dispersing hydration comprises applying an ultrasonic wave having a power of 50 W to 110 W. 8 . The method of claim 1 , wherein the ultrasonic wave dispersing hydration comprises applying an ultrasonic wave having a power to weight of 2.5 W/g to 5.5 W/g based on 1 g of aggregates. 9 . The method of claim 1 , wherein the ultrasonic wave dispersing hydration comprises applying an ultrasonic wave having a power to weight of 0.6 W/g to 1.4 W/g based on 1 g of the recovered transition metal slurry. 10 . The method of claim 1 , wherein the reduction treatment of the cathode active material particles is performed in a fluidized bed reactor using a reductive gas. 11 . The method of claim 1 , further comprising rehydrating the recovered transition metal slurry. 12 . The method of claim 1 , further comprising heat-treating the cathode active material particles at a temperature of 500° C. or less prior to performing the reduction treatment of the cathode active material particles.
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