Method for recovering lithium from waste lithium iron phosphate (LFP) material
This disclosure discloses a method for recovering lithium from a waste LFP material, including: S1. adding water to the waste LFP material, controlling a pH thereof at 0.5 to 2.0 and an ORP of the slurry at 0.05 V to 1.2 V, and filtering to obtain a material A; S2. adding sulfuric acid and heating a resulting mixture at 100° C. to 400° C. in the air or an oxygen atmosphere to obtain a material B; S3. adding water to the material B, and stirring and filtering to obtain a material C; S4. controlling a pH of the material C at 9 to 11, and filtering a resulting mixture to obtain a material D; S5. passing the material D through an ion-exchange resin to obtain a material E; and S6. adding the material E to a sodium carbonate solution to react; and collecting a resulting solid to obtain lithium carbonate.
1 . A method for recovering lithium from a waste lithium iron phosphate (LFP) material, comprising the following steps:
S1. adding water to the waste LFP material to prepare a slurry, controlling a pH of the slurry at 0.5 to 2.0 and an oxidation-reduction potential (ORP) of the slurry at 0.2V to 0.5V, and filtering the slurry to obtain a filter residue, which is an aluminum-free LFP power;
S2. adding sulfuric acid to the aluminum-free LFP power, and heating a resulting mixture at 100° C. to 400° C. in the air or an oxygen atmosphere to obtain a mixture of iron phosphate and lithium sulfate;
S3. adding water to the mixture of iron phosphate and lithium sulfate, and stirring and filtering to obtain a filtrate, which is a lithium sulfate solution;
S4. controlling a pH of the lithium sulfate solution at 9 to 11, and filtering to obtain a filtrate, which is a purified lithium sulfate solution;
S5. passing the purified lithium sulfate solution through an ion-exchange resin to obtain a further-purified lithium sulfate solution; and
S6. adding the further-purified lithium sulfate solution to a sodium carbonate solution to react; and collecting a resulting solid to obtain lithium carbonate;
wherein
in S2, the sulfuric acid has a mass concentration of 50% to 98%;
in S1, the ORP is controlled by adding sodium chlorate and/or hydrogen peroxide and the pH is controlled by adding a sulfuric acid solution or a hydrochloric acid solution.
2 . The method according to claim 1 , wherein in S2, the sulfuric acid is added at an amount such that a molar ratio of hydrogen ion to lithium in the resulting mixture is 1.0 to 1.5.
3 . The method according to claim 1 , wherein in S2, the heating is conducted for 1 h to 5 h.
4 . The method according to claim 1 , wherein in S2, the heating is conducted at 150° C. to 250° C.
5 . The method according to claim 1 , wherein in S4, the pH is adjusted by adding lithium carbonate and/or sodium carbonate.