Process for the recovery of metals from a Li-containing starting material

Patent metadata

Field	Value
Publication number	US-12170355-B2
Application number	US-202017603998-A
Country	US
Kind code	B2
Filing date	Apr 17, 2020
Priority date	Apr 19, 2019
Publication date	Dec 17, 2024
Grant date	Dec 17, 2024

Abstract

The invention concerns a process for the recovery of metals such as Ni and Co from a Li-containing starting material.
In particular, this process concerns the recovery of metals M from a Li-containing starting material, wherein M comprises Ni and Co, comprising the steps of:
Step 1: Providing said starting material, comprising Li-ion batteries or their derived products;
Step 2: Removing Li in an amount of more than the maximum of (1) 30% of the Li present in said starting material, and (2) a percentage of the Li present in said starting material determined to obtain a Li:M ratio of less than 0.70 in a subsequent acidic leaching step;

Step 3: Subsequent leaching using relative amounts of Li-depleted product and a mineral acid, thereby obtaining a Ni- and Co-bearing solution; and,

Step 4: Crystallization of Ni, Co, and optionally Mn.

Due to the lower reagent consumption and higher Ni and/or Co concentration during hydrometallurgical processing, the invention is an efficient and economic process for the production of crystals suitable for battery material production.

First claim

The invention claimed is:

1. A process for the recovery of metals M from a Li-containing starting material, wherein M comprises Ni and Co, comprising the steps of:
Step 1: Providing said starting material, comprising Li-ion batteries or their derived products;
Step 2: Removing Li in an amount of more than the maximum of (1) 30% of the Li present in said starting material, and (2) a percentage of the Li present in said starting material determined to obtain a Li:M ratio of 0.70 or less in a subsequent acidic leaching step, by using either one or more of:
a pyrometallurgical smelting process comprising heating and introducing a reducing agent and slag-formers, thereby producing one or more of a Li-bearing slag phase and Li-fumes, and a Li-depleted Ni—Co-bearing phase susceptible to be acid-leached;
a thermal treatment process comprising heating and introducing a reducing agent, thereby producing a Ni—Co-bearing residue containing at least one water-soluble Li-compound, and removing said at least one Li-compound by washing with an aqueous solution, thereby obtaining a Li-depleted Ni—Co-bearing residue susceptible to be acid-leached;
a hydrometallurgical leaching process comprising introducing an aqueous or acidic solution, thereby leaching Li from said starting material, wherein Ni and Co are at least partially insoluble, and solid-liquid separation, thereby obtaining a Li-depleted Ni—Co-bearing residue susceptible to be acid-leached;

Step 3: Subsequent leaching using relative amounts of Li-depleted Ni—Co-bearing material, obtained in step 2, and a mineral acid, thereby obtaining a Ni- and Co-bearing solution; and,
Step 4: Crystallization of Ni, Co, and optionally Mn, wherein step 4 is performed by lowering the temperature of the Ni- and Co-bearing solution and/or by removing water from the Ni- and Co-bearing solution and/or by solvent displacement crystallization.

2. The process according to claim 1 , wherein the thermal treatment process of step 2 is performed at a temperature above 250° C.

3. The process according to claim 1 , wherein the step of removing said at least one water-soluble Li-compound by washing with an aqueous solution is performed at a pH of 2.5 or higher.

4. The process according to claim 1 , wherein said at least one water-soluble Li-compound of step 2 comprises one or more of Li 2 O, Li 2 CO 3 , LiHCO 3 , LiCl, Li 2 SO 4 , LiF, LiOH.

5. The process according to claim 1 , wherein the mineral acid is one or more of HNO 3 , H 2 SO 4 and HCl.

6. The process according to claim 1 , wherein the Ni—Co-bearing phase of the pyrometallurgical smelting process of step 2 is comminuted to a particle size distribution with an average diameter of 10 mm or less.

7. The process according to claim 1 , wherein the Ni- and Co-bearing solution from step 3 also contains Cu and/or Fe and/or Al, wherein the process comprises a purification step between step 3 and step 4, wherein Cu and/or Fe and/or Al are removed from the Ni- and Co-bearing solution.

8. The process according to claim 1 , wherein the Ni- and Co-bearing solution from step 3 also contains Mn, wherein the process comprises a Mn-removal step between step 3 and step 4, wherein Mn is removed from the Ni- and Co-bearing solution.

9. The process according to claim 1 , wherein before step 4 the ratio of Ni to Co in the Ni- and Co-bearing solution is adjusted to a desired value by addition of Ni and/or Co in dissolved form or as one or more compounds which are soluble in the Ni- and Co-bearing solution.

10. The process according to claim 1 , wherein before step 4 the ratio of Ni to Co to Mn in the Ni- and Co-bearing solution is adjusted to a desired value by addition of one or more of Ni, Co, and Mn in a dissolved form or as one or more compounds which are soluble in the Ni- and Co-bearing solution.

11. The process according to claim 1 , wherein the Ni- and Co-bearing solution contains more Ni than Co, when expressed in g/l.

12. The process according to claim 1 , wherein the Ni- and Co-bearing solution contains more Ni than the sum of Co and Mn, when expressed in g/l.

13. The process according to claim 1 , comprising a purification step between step 3 and step 4, wherein Co is selectively removed from the Ni- and Co-bearing solution, resulting in a Co-depleted, Ni-bearing solution, suitable for obtaining Ni crystals.

14. The process according to claim 1 , wherein the starting material contains Ni, Co, Li, Al, F, and one or more of Cu and Fe, wherein the pyrometallurgical smelting process of step 2 is a reducing smelting of the starting material with fluxing agents, wherein the Ni—Co-bearing phase is an alloy comprising a major part of Ni, Co, Cu and at least part of the Fe and, wherein the alloy is depleted in Li, Al and F.

Assignees

• Umicore Nv

Inventors

• Verhees Pieter
• Klaasen Bart
• Callebaut Willem

Classifications

• C22B47/00

  Obtaining manganese · CPC title

• C22B26/12

  Obtaining lithium · CPC title

• C22B23/0415

  with acids or salt solutions except ammonium salts solutions · CPC title

• C22B7/007

  by acid leaching · CPC title

• C22B7/003

  only remelting, e.g. of chips, borings, turnings; apparatus used therefor · CPC title