Process for the recovery of cathode materials in the recycling of batteries by removing aluminum and iron

Patent metadata

Field	Value
Publication number	US-11509000-B2
Application number	US-202017601865-A
Country	US
Kind code	B2
Filing date	Apr 14, 2020
Priority date	Apr 15, 2019
Publication date	Nov 22, 2022
Grant date	Nov 22, 2022

Abstract

A process for removal of aluminium and iron in the recycling of rechargeable batteries comprising providing a leachate from black mass, adding phosphoric acid (H3PO4) to said leachate and adjusting the pH to form iron phosphate (FePO4) and aluminium phosphate (AlPO4), precipitating and removing the formed FePO4 and AlPO4, and forming a filtrate for further recovery of cathode metals, mainly NMC-metals and lithium.

First claim

The invention claimed is:

1. A process for removal of aluminum and iron from black mass in the recycling of rechargeable batteries, the aluminum being removed in the form of aluminum phosphate (AlPO 4 ) and the iron being removed in the form of iron phosphate (FePO 4 ), said process comprising:
providing a leachate from black mass,
adding phosphoric acid (H 3 PO 4 ) to the provided leachate,
adjusting the pH of the H 3 PO 4 containing leachate to form the (FePO 4 ) and the (AlPO 4 ,
precipitating and removing the formed FePO 4 and AlPO 4 from the pH adjusted H 3 PO 4 containing leachate, and
forming a filtrate for recovery of cathode metals.

2. The process according to claim 1 , wherein the rechargeable batteries are rechargeable lithium ion batteries.

3. The process according to claim 1 , wherein the precipitation is performed in two steps at different pH levels.

4. The process according to claim 3 , wherein the pH in a first precipitation step is adjusted to an interval of pH 1.5 to 4.

5. The process according to claim 4 , wherein the interval of pH is either: 1.5 to 3.5 or 1.5 to 3.

6. The process according to claim 3 , wherein the pH, in a second step, is adjusted to an interval of pH 2.5 to 6.5.

7. The process according to claim 6 , wherein the interval of pH is either: 2.5 to 6 or 2.5 to 4.

8. The process according to claim 3 , wherein crystallization seeds are added to precipitate FePO 4 and AlPO 4 in the first precipitation step.

9. The process according to claim 8 , wherein the crystallization seeds comprise aluminum and iron phosphate crystals and wherein said seeds are added in an amount of 0.05-0.3 g/L.

10. The process according to claim 9 , wherein the amount of added seeds is either 0.05-0.2 g/L or 0.05-0.15 g/L.

11. The process according to claim 3 , wherein the two precipitation steps are conducted at a temperature in an interval of 20-95° C.

12. The process according to claim 11 , wherein the temperature interval is either: 55-85° C. or 65-75° C.

13. The process according to claim 3 , wherein each of the two precipitation steps has a residence time in an interval of 2-24 hours.

14. The process according to claim 3 , wherein the residence time interval is one of: 12-18 h, 2-12 h, or 2-6 hours.

15. The process according to claim 3 , wherein a higher amount of FePO 4 and AlPO 4 is precipitated in a first precipitation step than in a second precipitation step.

16. The process according to claim 1 , wherein the precipitate comprising FePO 4 and AlPO 4 is washed with an aqueous solution having a pH in an interval of pH 1.5-5.5.

17. The process according to claim 1 , wherein the aqueous solution pH interval is 1.5-2.5.

18. The process according to claim 1 , wherein the filtrate comprises:
lithium, nickel, manganese and cobalt, and
less than 10 ppm of one or more of aluminum, iron, or copper.

19. The process according to claim 1 , wherein the leachate provided from the black mass is substantially copper free.

20. The process according to claim 1 , wherein copper is recovered subsequently to the removal of the aluminum in the form of the AlPO 4 and the iron in the form of the FePO 4 .

Assignees

• Northvolt Ab

Inventors

• Alemrajabi Mahmood
• Karlsson Ingrid
• Sjödahl Ragnar
• Nehrenheim Emma
• Petranikova Martina
• Tunsu Cristian

Classifications

• B09B3/30

  involving mechanical treatment (involving an extraction step B09B3/80) · CPC title

• C22B3/20

  Treatment or purification of solutions, e.g. obtained by leaching (C22B3/18 takes precedence) · CPC title

• C22B47/0081

  Treatment or purification of solutions, e.g. obtained by leaching (C22B47/0054 takes precedence) · CPC title

• H01M10/54 Primary

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B23/0461

  by chemical methods · CPC title