Fluidized bed reactor and method for recovering active metal of lithium secondary battery utilizing same
US-2022395794-A1 · Dec 15, 2022 · US
US2022349022A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022349022-A1 |
| Application number | US-202217855444-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 30, 2022 |
| Priority date | Dec 30, 2019 |
| Publication date | Nov 3, 2022 |
| Grant date | — |
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A method of recovering an active metal of a lithium secondary battery according to an embodiment of the present invention includes preparing a waste cathode active material mixture obtained from a waste cathode of a lithium secondary battery, forming a preliminary precursor mixture by reacting the waste cathode active material mixture with a reactive gas in a fluidized bed reactor, and selectively recovering a lithium precursor from the preliminary precursor mixture. The fluidized bed reactor includes a reactor body and a horizontal expansion bed, and a ratio of a diameter of the horizontal expansion bed relative to a diameter of the reactor body is 3 or more to improve a recovery efficiency of a lithium secondary battery.
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What is claimed is: 1 . A method of recovering an active metal of a lithium secondary battery, the method comprising: preparing a waste cathode active material mixture obtained from a waste cathode of a lithium secondary battery; forming a preliminary precursor mixture by reacting the waste cathode active material mixture with a reactive gas in a fluidized bed reactor; and selectively recovering a lithium precursor from the preliminary precursor mixture, wherein the fluidized bed reactor comprises a reactor body and a horizontal expansion bed; and a ratio of a diameter of the horizontal expansion bed relative to a diameter of the reactor body is 3 or more. 2 . The method of claim 1 , wherein the forming of the preliminary precursor mixture comprises lowering the waste cathode active material mixture or the preliminary precursor mixture raised from the reactor body to the horizontal expansion bed by the reactive gas to be gathered in the reactor body. 3 . The method of claim 1 , wherein the ratio of the diameter of the horizontal expansion bed relative to the diameter of the reactor body is from 3 to 10. 4 . The method of claim 1 , wherein the fluidized bed reactor further comprises a vertical expansion tube connecting the reactor body and the horizontal expansion bed. 5 . The method of claim 4 , wherein an inclination angle of the vertical expansion tube is from 45 to 80°. 6 . The method of claim 1 , wherein the reactive gas comprises hydrogen. 7 . The method of claim 1 , wherein the recovering of the lithium precursor comprises washing the preliminary precursor mixture with water. 8 . A fluidized bed reactor, comprising: a reactor body; a horizontal expansion bed connected with the reactor body, the horizontal expansion bed having a diameter of at least three times a diameter of the reactor body; a vertical expansion tube connecting the reactor body and the horizontal expansion bed; and a gas injection path for injecting a reactive gas into the reactor body.
by reduction in solid state, e.g. by segregation processes · CPC title
Details of the fluidised bed reactor (B01J8/1836 takes precedence) · CPC title
the fluidising gas being a reactant · CPC title
Dry processes · CPC title
according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title
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