Recovery of critical elements from end-of-life lithium ion batteries with supported membrane solvent extraction

Patent metadata

Field	Value
Publication number	US-11811035-B2
Application number	US-202016884189-A
Country	US
Kind code	B2
Filing date	May 27, 2020
Priority date	May 27, 2020
Publication date	Nov 7, 2023
Grant date	Nov 7, 2023

Abstract

Single-stage and multi-stage systems and methods for the recovery of critical elements in substantially pure form from lithium ion batteries are provided. The systems and methods include supported membrane solvent extraction using an immobilized organic phase within the pores of permeable hollow fibers. The permeable hollow fibers are contacted by a feed solution on one side, and a strip solution on another side, to provide the simultaneous extraction and stripping of elements from dissolved lithium ion cathode materials, while rejecting other elements from the feed solution. The single- and multi-stage systems and methods can selectively recover cobalt, manganese, nickel, lithium, aluminum and other elements from spent battery cathodes and are not limited by equilibrium constraints as compared to traditional solvent extraction processes.

First claim

The invention claimed is:

1. A method for the recovery of cobalt from lithium ion batteries, the method comprising:
dissolving a battery material containing Co, Mn, Ni, and Li within an acid to form a feed solution, the feed solution including Co and Li;
providing a membrane module including a plurality of hollow fibers, the plurality of hollow fibers including a porous sidewall defining a lumen side spaced apart from a shell side;
wetting the porous sidewall of the plurality of hollow fibers with an organic phase, the organic phase including a cationic extractant and an organic solvent, wherein the organic phase is free of tributyl phosphate;
performing membrane solvent extraction by moving the feed solution along one of the lumen side or the shell side of the plurality of hollow fibers and simultaneously moving a strip solution along the other of the lumen side or the shell side of the plurality of hollow fibers, the strip solution including a pH that is less than a pH of the aqueous feed solution;
maintaining a pH of the feed solution within a predetermined range of between 4.0 and 6.0, inclusive, by intermittently introducing a buffer or a base to the feed solution during membrane solvent extraction;
wherein wetting the porous sidewall of the plurality of hollow fibers with the organic phase is performed prior to moving the feed solution and moving the strip solution, and wherein the cationic extractant in the porous sidewall continuously extracts Co and Mn from the aqueous feed solution for recovery by the strip solution while substantially rejecting Li and Ni.

2. The method of claim 1 wherein the feed solution includes a positive pressure differential with respect to the strip solution of between 1 psi and 5 psi.

3. The method of claim 1 wherein the feed solution and the strip solution are moving in continuous recirculation through the membrane module for at least thirty minutes.

4. The method of claim 1 further including separating the battery material from a spent battery cathode, wherein separating the battery material from a spent battery cathode includes subjecting the spent battery cathode to a thermal treatment, acid dissolution, and vacuum filtration.

5. The method of claim 1 , wherein the cationic extractant is a virgin cation extractant in hydrogen form.

6. A method for recycling battery material, the method comprising:
dissolving battery material containing Co, Mn, Li, and Ni within an acid to form a first feed solution and regulating the pH of the first feed solution between 4 and 6, inclusive;
providing a first membrane module including a first plurality of hollow fibers, the first plurality of hollow fibers each including a lumen side and a shell side;
wetting the first plurality of hollow fibers with a first organic phase, the first organic phase including a first cationic extractant and being free of tributyl phosphate; and
after wetting the first plurality of hollow fibers, moving the aqueous feed solution along one of the lumen side or the shell side of the plurality of hollow fibers and simultaneously moving a strip solution along the other of the lumen side or the shell side of the plurality of hollow fibers;
wherein the first cationic extractant continuously removes Co and Mn from the aqueous feed solution as a first-stage membrane solvent extraction while substantially rejecting Li and Ni, and wherein the strip solution continuously back extracts Co and Mn from the first organic phase.

7. The method of claim 6 wherein regulating the pH of the first feed solution includes intermittently adding a buffer or a base to maintain the pH between 4 and 6, inclusive.

8. The method of claim 6 wherein the first feed solution includes a positive pressure differential with respect to the first strip solution of between 1 psi and 5 psi.

9. The method of claim 6 wherein moving the first feed solution and moving the first strip solution includes continuously recirculating the first feed solution and the first strip solution through the first membrane module for at least one hour.

10. The method of claim 6 wherein first plurality of hollow fibers are formed from a porous hydrophobic material.

11. The method of claim 6 further including separating the battery material from a spent battery cathode, wherein separating the battery material from a spent battery cathode includes subjecting the spent battery cathode to a thermal treatment, acid dissolution, and vacuum filtration.

12. The method of claim 6 , wherein the first cationic extractant is a virgin cation extractant in hydrogen form.

13. A method for recycling battery material, the method comprising:
dissolving battery material containing Co, Mn, Li, and Ni within an acid to form a first feed solution and regulating the pH of the first feed solution between 4 and 6, inclusive;
providing a first membrane module including a first plurality of hollow fibers, the first plurality of hollow fibers each including a lumen side and a shell side;
wetting the first plurality of hollow fibers with a first organic phase, the first organic phase including a first cationic extractant; and
after wetting the first plurality of hollow fibers, moving the aqueous feed solution along one of the lumen side or the shell side of the plurality of hollow fibers and simultaneously moving a strip solution along the other of the lumen side or the shell side of the plurality of hollow fibers;
wherein the first cationic extractant continuously removes Co and Mn from the aqueous feed solution as a first-stage membrane solvent extraction while substantially rejecting Li and Ni, and wherein the strip solution continuously back extracts Co and Mn from the first organic phase;
further including performing a second-stage membrane solvent extraction of the first strip solution, as a second feed solution, to recover Co while substantially rejecting Mn, and regulating the pH of the second feed solution to be less than or equal to 1.5.

14. The method of claim 13 wherein the second-stage membrane solvent extraction includes:
providing a second membrane module including a second plurality of hollow fibers, the second plurality of hollow fibers including a lumen side and a shell side;
wetting the second plurality of hollow fibers with a second organic phase, the second organic phase including a second cationic extractant; and
moving the second feed solution along one of the lumen side or the shell side of the second plurality of hollow fibers and simultaneously moving a second strip solution along the other of the lumen side or the shell side of the second plurality of hollow fibers;
wherein the second cationic extractant continuously extracts Co from the second feed solution while substantially rejecting Mn, and wherein the third strip solution continuously back extracts Co from the second organic phase.

15. The method of claim 13 further including performing a third-stage membrane solvent extraction of the first solution, as a third feed solution, to recover Ni while substantially rejecting Li, and regulating the pH of the third feed solution to be between 6.0 and 6.5, inclusive.

16. The method of claim 15 wherein the third-stage membrane solvent extraction includes:
providing a third membrane module including a third plurality of hollow fibers, the third plurality of hollow fibers including a lumen side and a shell side;
wetting the third plurality of hollow fibers with a third organic phase, the third organic phase including a third cationic extractant; and
moving the third feed solution along one of the lumen side or the shell side of the third

Assignees

• Ut Battelle Llc

Inventors

• Bhave Ramesh R
• Islam Syed Z
• Wagh Priyesh A

Classifications

• B01D2325/0283

  Pore size · CPC title

• H01M10/54 Primary

  Reclaiming serviceable parts of waste accumulators · CPC title

• B01D63/02 Primary

  Hollow fibre modules · CPC title

• B01D11/0415

  in combination with membranes · CPC title

• B01D11/0488

  Flow sheets · CPC title