Fluidized bed reactor and method for recovering active metal of lithium secondary battery by using same
US-2025207217-A1 · Jun 26, 2025 · US
US2023238599A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023238599-A1 |
| Application number | US-202117929000-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 28, 2021 |
| Priority date | Jun 1, 2020 |
| Publication date | Jul 27, 2023 |
| Grant date | — |
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In a method for recovering active metals from a lithium secondary battery according to exemplary embodiments, a cathode active material mixture including a lithium composite oxide may be reacted with a reducing reaction gas under a pressurized condition and washed with water. In this case, a large amount of the cathode active material mixture may be treated within a shortened process time, and the active metal may be recovered with high yield and high efficiency.
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1 . A method for recovering an active metal from a lithium secondary battery, the method comprising: preparing a cathode active material mixture including a lithium composite oxide from a waste cathode of the lithium secondary battery; forming a preliminary precursor mixture by reacting the cathode active material mixture with a reducing reaction gas under a pressurized condition of 3 bar to 25 bar; and recovering a lithium precursor by performing water washing treatment on the preliminary precursor mixture. 2 . The method according to claim 1 , wherein a reaction temperature with the reducing reaction gas is 420° C. to 500° C. 3 . The method according to claim 1 , wherein the step of reacting with the reducing reaction gas comprises supplying the reducing reaction gas into a reactor in a reaction time of less than 1 hour at 5 to 50 mL/min/g of cathode active material. 4 . The method according to claim 1 , wherein the reaction with the reducing reaction gas is performed in a fixed bed reactor or a fluidized bed reactor. 5 . The method according to claim 1 , wherein the reducing reaction gas includes hydrogen and a carrier gas, and a concentration of the hydrogen in the reducing reaction gas is 10 to 40 volume %. 6 . The method according to claim 5 , wherein the carrier gas includes nitrogen or argon. 7 . The method according to claim 1 , wherein the step of preparing of the cathode active material mixture comprises dry pulverizing the waste cathode. 8 . The method according to claim 1 , wherein the lithium composite oxide contains nickel (Ni), cobalt (Co) and manganese (Mn). 9 . The method according to claim 7 , wherein the preliminary precursor mixture comprises preliminary lithium precursor particles and transition metal-containing particles, and the transition metal-containing particles include Ni-containing particles, Co-containing particles and Mn-containing particles. 10 . The method according to claim 9 , further comprising precipitating the transition metal-containing particles through the water washing treatment. 11 . The method according to claim 9 , further comprising recovering a transition metal precursor in a form of an acid salt by selectively treating the transition metal-containing particles with an acid solution.
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