Processing hard rock lithium minerals or other materials to produce lithium materials and byproducts converted from a sodium sulfate intermediate product
US-2024425381-A1 · Dec 26, 2024 · US
US2025207217A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025207217-A1 |
| Application number | US-202519078298-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 13, 2025 |
| Priority date | Sep 13, 2022 |
| Publication date | Jun 26, 2025 |
| Grant date | — |
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A method for recovering active metals of a lithium secondary battery may supply a cathode active material mixture to a fluidized bed reactor including a reactor body. A reaction gas may be introduced from a lower portion of the fluidized bed reactor to form a fluidized bed including a preliminary precursor mixture within the reactor body. The fluidized bed portion that has entered the upper portion of the fluidized bed reactor may be cooled to descend it into the reactor body, and then a lithium precursor may be recovered from the preliminary precursor mixture. Accordingly, a terminal velocity of the preliminary precursor is reduced, such that even if the particle size of the preliminary precursor is fine, loss due to scattering may be prevented.
Opening claim text (preview).
1 . A method for recovering active metals of a lithium secondary battery, comprising: supplying a cathode active material mixture to a fluidized bed reactor including a reactor body; introducing a reaction gas from a lower portion of the fluidized bed reactor to form a fluidized bed including a preliminary precursor mixture within the reactor body; cooling the fluidized bed portion that has entered an upper portion of the fluidized bed reactor to descend it into the reactor body; and recovering a lithium precursor from the preliminary precursor mixture. 2 . The method for recovering active metals of a lithium secondary battery according to claim 1 , wherein the fluidized bed reactor comprises an expansion chamber connected to the reactor body, and an intermediate part formed between the reactor body and the expansion chamber to connect them, and cooling the fluidized bed portion is performed within the expansion chamber. 3 . The method for recovering active metals of a lithium secondary battery according to claim 2 , wherein cooling the fluidized bed portion is performed through a cooling jacket which surrounds an outer wall of the expansion chamber. 4 . The method for recovering active metals of a lithium secondary battery according to claim 2 , wherein cooling the fluidized bed portion is performed through a cooling coil or cooling fins disposed inside the expansion chamber. 5 . The method for recovering active metals of a lithium secondary battery according to claim 4 , wherein cooling the fluidized bed portion comprises bringing the cooling coil into contact with the fluidized bed portion that has ascended to the expansion chamber. 6 . The method for recovering active metals of a lithium secondary battery according to claim 2 , wherein cooling the fluidized bed portion comprises directly injecting a coolant into the expansion chamber. 7 . The method for recovering active metals of a lithium secondary battery according to claim 2 , wherein the intermediate part comprises an inclined side wall extending from an end of the reactor body to the expansion chamber. 8 . The method for recovering active metals of a lithium secondary battery according to claim 1 , wherein an internal temperature of the expansion chamber is maintained lower than that of the reactor body. 9 . The method for recovering active metals of a lithium secondary battery according to claim 8 , wherein the internal temperature of the expansion chamber is 20 to 300° C., and the internal temperature of the reactor body is 400 to 700° C. 10 . The method for recovering active metals of a lithium secondary battery according to claim 1 , wherein cooling the fluidized bed portion that has entered the upper portion of the fluidized bed reactor comprises reducing a moving velocity of particles included in the preliminary precursor mixture to a terminal velocity or less. 11 . A fluidized bed reactor comprising: a reactor body; an expansion chamber connected to an end of the reactor body and having a width greater than that of the reactor body; and a coolant injection port fixed to an upper surface of the expansion chamber to directly inject a coolant to a reactant. 12 . The fluidized bed reactor according to claim 11 , further comprising an intermediate part which is formed between the reactor body and the expansion chamber to connect them, and includes an inclined side wall. 13 . The fluidized bed reactor according to claim 12 , wherein an inclination angle between an imaginary line extending in a direction perpendicular to the side of the reactor body and the inclined side wall is 30° to 80°. 14 . The fluidized bed reactor according to claim 11 , further comprising a reactor lower portion connected to a bottom portion of the reactor body, a fluid inlet configured to inject a reaction gas into the reactor lower portion, and a fluid outlet connected to the expansion chamber to discharge the reaction gas. 15 . The fluidized bed reactor according to claim 14 , further comprising a dispersion plate which divides the reactor lower portion and the reactor body. 16 . A method for recovering active metals from a cathode active material of a lithium secondary battery, comprising: supplying the cathode active material and a reaction gas into a fluidized bed reactor including a reactor body, an expansion chamber and an intermediate part coupling the reactor body to the expansion chamber; forming a fluidized bed including a preliminary precursor mixture within the reactor body; cooling a fluidized bed portion entering the expansion chamber of the fluidized bed reactor to cause it to descend into the reactor body; and recovering a lithium precursor from the preliminary precursor mixture.
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