Carbon anode for lithium ion electrochemical cell

• US 5,700,298 A
• Filed: 03/15/1996
• Issued: 12/23/1997
• Est. Priority Date: 03/15/1996
• Status: Expired due to Term

• Current Assignee: Valence Technology Incorporated (Lithium Werks B.V.)
• Original Assignee: Valence Technology Incorporated (Lithium Werks B.V.)
• Inventors: Shi, Hang, Barker, Jeremy, Koksbang, Rene
• Primary Examiner(s): Gorgos, Kathryn L.
• Assistant Examiner(s): Wong, Edna
• Application Number:
  US08/616,826
• Time in Patent Office: 648 Days
• Field of Search: 429/232, 423/448, 29/623.1, 204/294
• US Class Current: 29/623.1
• CPC Class Codes: C01B 32/22 Intercalation
• CPC Class Codes: H01M 10/0525 Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
• CPC Class Codes: H01M 2004/021 Physical characteristics, e.g. porosity, surface area
• CPC Class Codes: H01M 4/1393 of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
• CPC Class Codes: H01M 4/587 for inserting or intercalating light metals
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y10T 29/49108 Electric battery cell making

Abstract

Increasing the percentage of the 3R phase present in graphite reduces the first capacity loss of anodes employing the so modified graphite. Conversion of 2H phase graphite to 3R phase graphite can be achieved by grinding graphite. Non-aqueous solid electrochemical cells with improved performance can be fabricated by employing intercalation based carbon anodes comprising graphite with high percentage of 3R. When employed in an electrochemical cell, the first cycle capacity loss of only about 10%.

Claims

1. A method of preparing an electrochemical cell and controlling the first cycle capacity loss of said electrochemical cell, which method comprises the steps of:

(a) forming an intercalation based anode comprising graphite particles by a process comprising;

(i) providing an initial graphite composition;

(ii) measuring the percentage of 3R phase graphite present in said initial graphite composition;

(iii) increasing the percentage of 3R phase graphite in said initial graphite composition to form a second graphite composition which comprises graphite particles having an average diameter of less than 75 μ

m;

(b) providing a cathode; and

(c) interposing a non-aqueous electrolyte containing a solvent and lithium salt between the anode and cathode.

2. The method of claim 1 wherein the step of increasing the percentage of 3R phase graphite comprises:

converting graphite in the 2H phase to graphite in the 3R phase.

3. The method of claim 2 wherein the step of converting the graphite forms graphite particles in said second graphite composition wherein the percentage of 3R phase graphite is at least about 30 percent.

4. The method of claim 1 wherein the step of increasing the percentage of 3R phase graphite comprises:

grinding said initial graphite composition to convert graphite in the 2H phase to the 3R phase.

5. The method of claim 4 wherein grinding said initial graphite composition produces particles having an average diameter in the range of about 5 to about 15 μ

m.

6. The method of claim 1 wherein the cathode comprises cathode active materials selected from lithiated cobalt oxides, lithiated manganese oxides, lithiated nickel oxides, lithiated vanadium oxides, and mixtures thereof.

7. A method of preparing an electrochemical cell and reducing the first capacity loss of said electrochemical cell, which method comprises the steps of:

(a) forming an intercalation based anode comprising graphite particles by a process comprising;

(i) providing an initial graphite composition;

(ii) increasing the percentage of 3R phase graphite present in said initial graphite composition to form a second graphite composition which comprises graphite wherein at least 20 percent of the graphite is 3R phase graphite;

(b) providing a cathode; and

(c) interposing a non-aqueous electrolyte containing a solvent and lithium salt between the anode and cathode and wherein the electrochemical cell has a first cycle loss of less than about 15% and a specific capacity of greater than 300 mAh/g.

8. The method of claim 7 wherein the step of increasing the percentage of 3R phase graphite forms graphite particles wherein the percentage of 3R phase graphite is at least about 30 percent.

9. The method of claim 7 wherein the step of increasing the percentage of 3R phase graphite comprises:

grinding said initial graphite composition to convert graphite in the 2H phase to the 3R phase.

10. The method of claim 9 wherein grinding said initial graphite composition produces graphite particles having an average diameter in the range of about 5 to about 15 μ

m.

11. The method of claim 7 wherein the cathode comprises cathode active materials selected from lithiated cobalt oxides, lithiated manganese oxides, lithiated nickel oxides, lithiated vanadium oxides, and mixtures thereof.

12. A method of preparing an intercalation based carbon anode comprising graphite particles and controlling the first cycle capacity loss when employed in an electrochemical cell, which method comprises the steps of:

providing an initial graphite composition;

measuring the percentage of 3R phase graphite present in said initial graphite composition; and

increasing the percentage of 3R phase graphite in said initial graphite composition to form a second graphite composition which comprises graphite particles having an average diameter of less than 75 μ

m wherein the second graphite composition has a lower first cycle capacity loss than the initial graphite composition when employed in the electrochemical cell.

13. The method of claim 12 wherein the step of increasing the percentage of 3R phase graphite comprises:

converting graphite in the 2H phase to graphite in the 3R phase.

14. The method of claim 13 wherein the step of converting the graphite forms graphite particles in said second graphite composition wherein the percentage of 3R phase graphite is at least about 30 percent.

15. The method of claim 12 wherein the step of increasing the percentage of 3R phase graphite particles comprises:

grinding said graphite composition to convert graphite in the 2H phase to the 3R phase.

16. The method of claim 15 wherein grinding said initial graphite composition produces graphite particles having an average diameter in the range of about 5 to about 15 μ

m.

17. A method of preparing an intercalation based carbon anode comprising graphite wherein the anode has less than about 10 percent first cycle capacity loss when employed in an electrochemical cell, which method comprises the steps of:

providing an initial graphite composition; and

increasing the percentage of 3R phase graphite in said initial graphite composition to form a second graphite composition which comprises graphite wherein at least about 20 percent of the graphite is 3R phase graphite wherein the second graphite composition has a lower first cycle capacity loss than the initial graphite composition when employed in the electrochemical cell.

18. The method of claim 17 wherein the step of increasing the percentage of 3R phase graphite forms graphite particles wherein the percentage of 3R phase graphite in the graphite particles is at least about 30 percent.

19. The method of claim 17 wherein the step of increasing the percentage of 3R phase graphite comprises:

grinding said initial graphite composition to convert graphite in the 2H phase to the 3R phase.

20. The method of claim 19 wherein grinding said initial graphite composition produces graphite particles having an average diameter in the range of about 5 to about 15 μ

m.