IP Library › Granted Patent US 12,431,505
Granted Patent B2
US 12,431,505 · App. 18/520,178 · Granted Sep 30, 2025

Dry electrode for energy storing devices

Inventors: Mitchell Miller (Mission, CA); Ali Khosrozadeh (Abbotsford, CA); Behzad Gorji Pour Shafiee (Abbotsford, CA); Omar Khaled Omar Bin Gah (Abbotsford, CA); Mohsen Sadeghi (Abbotsford, CA)
Assignee: Atlas Power Technologies Inc.
H01M4/623H01M4/0404H01M4/0435H01M4/0471H01M4/364H01M4/587H01M4/661H01M10/0431H01M2004/021
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Quick Facts
Patent No.
US 12,431,505
App. No.
18/520,178
Granted
Sep 30, 2025
Kind
B2
Abstract

Electrical energy storage devices made using a wet electrode application technique are associated with high energy consumption. Herein, a dry electrode or electrolyte application process involves mixing activated carbon with a binder and then fibrillating the mixture. The mixture is roll-pressed into a film, which is then actively cooled. Optionally, tension in the cooled portion of the film is increased for spooling the film. The film is adhered to a pre-treated current collector and then wound into a jelly roll for the manufacture of an electrical energy storage device.

Claims (73)

1. A process for manufacturing a film for an energy storage device, comprising:

mixing dry, powdered active material with a binder to form a mixture;

fibrillating the mixture, thereby forming a fibrillated mixture;

sieving the fibrillated mixture, thereby forming a sieved, fibrillated mixture;

heating the sieved, fibrillated mixture between rollers to form the film, the rollers being at a temperature between 50° C. and 160° C.; and

actively cooling the film to between 10° C. and 70° C. within a distance of 30 cm from a location of formation of the film, resulting in a cooled film;

wherein the film is a dry electrode film or a dry electrolyte film.

2. The process of claim 1 , wherein:

the film is the dry electrode film;

the dry, powdered active material is activated carbon; and

the binder is PTFE (polytetrafluoroethylene).

3. The process of claim 2 , further comprising mixing carbon black with the activated carbon and the binder, the carbon black being present in the mixture from over 0% to 20% by weight.

4. The process of claim 1 , wherein:

the mixture comprises 1-30% by weight of the binder, and

the binder is PTFE (polytetrafluoroethylene).

5. The process of claim 1 , wherein:

the mixture comprises 10-15% by weight of the binder; and

the binder is PTFE (polytetrafluoroethylene).

6. The process of claim 1 , wherein the mixture comprises by weight:

50-99% of the dry, powdered active material;

1-30% of the binder, and

0-20% of a conductive additive.

7. The process of claim 1 , wherein the mixture comprises by weight:

75-98% of the dry, powdered active material;

2-15% of the binder, and

0-10% of a conductive additive.

8. The process of claim 1 , wherein the mixture comprises by weight:

80-95% of the dry, powdered active material, the dry, powdered active material being activated carbon;

1.5-15% of the binder, the binder being a fluoropolymer, and

0-15% of a conductive additive.

9. The process of claim 1 , wherein the mixture comprises by weight:

5-20% of the binder, the binder being a fluoropolymer.

10. The process of claim 1 , comprising passing the fibrillated mixture over a vibrating surface before said sieving, said sieving being through a vibrating sieve.

11. The process of claim 1 , wherein the film is actively cooled with a current of chilled gas.

12. The process of claim 1 , wherein the film is actively cooled with a chilled roller.

13. The process of claim 1 , further comprising trimming the cooled film to result in a trimmed, cooled film.

14. The process of claim 1 , further comprising:

trimming the cooled film to result in a trimmed, cooled film;

applying a first tension to the film, the cooled film and a first portion of the trimmed, cooled film that is adjacent to the cooled film; and

applying a second tension to a second portion of the trimmed, cooled film;

wherein the second tension is greater than the first tension.

15. The process of claim 14 , further comprising spooling the trimmed, cooled film under the second tension.

16. The process of claim 15 , wherein the trimmed, cooled film is uncalendered.

17. The process of claim 14 , wherein:

the first tension is between 6.7μN-0.13N per mm 2 cross-section of the second portion of the trimmed, cooled film; and

the second tension is between 0.033N-0.4N per mm 2 cross-section of the second portion of the trimmed, cooled film.

18. The process of claim 13 , further comprising adhering at least some of the trimmed, cooled film to an aluminum foil.

19. The process of claim 18 , further comprising prior to said adhering:

removing oil residue from the aluminum foil; and

applying adhesive to the aluminum foil.

20. The process of claim 19 , wherein the aluminum foil is heated to between 50° C. and 200° C. to remove the oil residue.

21. The process of claim 19 , comprising drying the applied adhesive prior to said adhering.

22. The process of claim 18 , comprising winding, in layers, into a jelly roll:

a first piece of the aluminum foil with the adhered, trimmed, cooled film;

a first separator;

a second piece of the aluminum foil with the adhered, trimmed, cooled film; and

a second separator.

23. The process of claim 22 , comprising manufacturing the energy storage device using the jelly roll.

24. The process of claim 1 , further comprising depositing the sieved, fibrillated mixture between the rollers to a height that is not greater than uppermost points of the rollers.

25. The process of claim 1 , wherein the fibrillated mixture is sieved through a 3-10 mm mesh.

26. The process of claim 1 , wherein a maximum dwell time of the sieved, fibrillated mixture between the rollers is 5 minutes.

27. The process of claim 1 , wherein a maximum dwell time of the sieved, fibrillated mixture between the rollers is 1 minute.

28. The process of claim 1 , wherein a maximum dwell time of the sieved, fibrillated mixture between the rollers is 30 seconds.

29. The process of claim 1 comprising mixing a non-aqueous lubricant with the dry, powdered active material and the binder to form the mixture.

30. The process of claim 1 comprising mixing a conductive additive with the dry, powdered active material and the binder to form the mixture.

31. The process of claim 1 , wherein the rollers are at a temperature between 80° C. and 140° C.

32. The process of claim 1 , wherein the film is actively cooled to below 25° C.

33. The process of claim 14 , wherein the mixture comprises by weight:

10-15% of the binder, the binder being PTFE (polytetrafluoroethylene).

34. The process of claim 1 , wherein:

the film is the dry electrolyte film;

the dry, powdered active material comprises an ion-conducting inorganic ceramic oxide, a Li-superionic conductor, a sodium superionic conductor, lithium sulfide, lithium sulfide boron sulfide, lithium germanium sulfide, polyethylene oxide (PEO), polyvinylidene fluoride (PVDF), poly (vinylidene fluoride-co-hexafluoropropylene) (PVDF-HFP), polyethylene glycol (PEG), LiTFSi, LiCIO 4 , LiPF 6 , or any combination selected therefrom; and

the binder is PTFE (polytetrafluoroethylene).

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 4, 2023
From: MILLER, MITCHELL; KHOSROZADEH, ALI; GORJI POUR SHAFIEE, BEHZAD; SADEGHI, MOHSEN; BIN GAH, OMAR KHALED OMAR
To: ATLAS POWER TECHNOLOGIES
Reel/Frame 065749/0191 →
Continuity (1)
Related Publication 20250174663A1 · May 29, 2025
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