Application of metal ion complexing agent in waste and old lithium iron phosphate battery recovery process
A technology of lithium iron phosphate battery and waste lithium battery, which is applied in the direction of waste collector recycling, lithium carbonate;/acid carbonate, etc., can solve the problems of low purity, limited reuse, etc., and achieves simple process operation, The effect of cost controllable and wide source of raw materials
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Embodiment 1
[0041] This embodiment provides a method for recycling waste lithium iron phosphate batteries, comprising the following steps:
[0042] S101: LiFePO will be scrapped 4 After the battery is discharged, mechanically disassembled and stripped, ultrasonically dispersed, and sieved, the black powder mixed with graphite powder and lithium iron phosphate is obtained.
[0043] S102: Dissolve 50 g of the above black powder in 125 mL of 2mol / L hydrochloric acid and 15 mL of 30% H 2 o 2 In the compound solution, heat and stir at 80°C for 2h, cool and stand still, and filter to obtain the filtrate containing Li and Fe and graphite powder.
[0044] S103: Add 50mL of 1000ppm Fe(NO 3 ) 3 Solution, and by adding NaOH solution to adjust the pH value of the system to 4, to obtain phosphate precipitate and filtrate.
[0045] S104: Add lye to the filtrate obtained in S103 to adjust the pH value to 10, and then remove the residual metal ion complexing agent to obtain a Li-containing + enrich...
Embodiment 2
[0049] This embodiment provides a method for recycling waste lithium iron phosphate batteries, comprising the following steps:
[0050] S101: LiFePO will be scrapped 4 After the battery is discharged, mechanically disassembled and stripped, ultrasonically dispersed, and sieved, the black powder mixed with graphite powder and lithium iron phosphate is obtained.
[0051] S102: Dissolve 100g of the above black powder in 250mL of 2mol / L HNO 3 solution with 30mL of 30% H 2 o 2 In the compound solution, heat and stir at 75°C for 3h, cool and stand still, and filter to obtain the filtrate containing Li and Fe and graphite powder.
[0052] S103: Add 80mL of 1000ppm Fe to the filtrate containing Li and Fe 2 (SO 4 ) 3 Solution, and by adding NaOH solution to adjust the pH value of the system to 3, to obtain phosphate precipitate and filtrate.
[0053] S104: Add lye to the filtrate obtained in S103 to adjust the pH value to 12, and then remove the residual metal ion complexing age...
Embodiment 3
[0058] This embodiment provides a method for recycling waste lithium iron phosphate batteries, comprising the following steps:
[0059] S101: LiFePO will be scrapped 4 After the battery is discharged, mechanically disassembled and stripped, ultrasonically dispersed, and sieved, the black powder mixed with graphite powder and lithium iron phosphate is obtained.
[0060] S102: Dissolve 100g of the above black powder in 250mL of 2mol / L H 2 SO 4 solution with 30mL of 30% H 2 o 2 In the compound solution, heat and stir at 80°C for 5h, cool and stand still, and filter to obtain the filtrate containing Li and Fe and graphite powder.
[0061] S103: Add 100mL of 1000ppm Fe(NO 3 ) 3 Solution, and by adding NaOH solution to adjust the pH value of the system to 2, to obtain phosphate precipitate and filtrate.
[0062] S104: Add lye to the filtrate obtained in S103 to adjust the pH value to 9, and then remove the residual metal ion complexing agent to obtain a Li-containing + enric...
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