Fuel gauge for an alkali metal electrochemical cell

• US 6,377,850 B1
• Filed: 03/09/2000
• Issued: 04/23/2002
• Est. Priority Date: 03/09/2000
• Status: Expired due to Term

• Current Assignee: Greatbatch Limited (Greatbatch Incorporated)
• Original Assignee: Wilson Greatbatch Technologies, Inc.
• Inventors: Syracuse, Kenneth C., Waite, Noelle M., Takeuchi, Esther S.
• Primary Examiner(s): Schaetzle, Kennedy
• Application Number:
  US09/522,327
• Time in Patent Office: 775 Days
• Field of Search: 607/2, 607/27, 607/28, 607/1, 607/29, 320/127, 320/134, 320/135, 320/136, 320/132, 320/161, 340/636, 324/427, 324/426
• US Class Current: 607/2
• CPC Class Codes: H01M 10/052 Li-accumulators
• CPC Class Codes: H01M 4/583 Carbonaceous material, e.g. graphite-intercalation compounds or CFx
• CPC Class Codes: H01M 4/5835 Comprising fluorine or fluoride salts
• CPC Class Codes: H01M 6/16 with organic electrolyte H01M6/18 takes precedence
• CPC Class Codes: H01M 6/5055 End of discharge indicated by a voltage step
• CPC Class Codes: Y02E 60/10 Energy storage using batteries

Abstract

A “fuel gauge” for a pulse dischargeable alkali metal/solid cathode cell is described. The rate of voltage recovery is used to determine the state of charge of the cell. Voltage recovery includes recovery from one load to a second, lighter load, or a loaded condition to OCV. The present invention is particularly useful as an end-of-life indicator for a Li/CF_x cell powering an implantable medical device.

Claims

1. In combination with an implantable medical device requiring a substantially constant discharge rate during a medical device monitoring function and at least one pulse discharge for a medical device operating function, the combination comprising:

a) an electrochemical cell comprising an alkali metal anode and a solid cathode activated with a nonaqueous electrolyte wherein the cell has a determinable stoichiometric capacity;

b) electronic circuitry powered by the electrochemical cell for discharging the cell under a first load condition and at a second, lighter load or at an open circuit voltage condition, wherein the first load occurs during a medical device operating mode for charging a capacitor or delivering therapy and the second load occurs during a medical device monitoring mode; and

c) wherein the electronic circuitry provides for determining the remaining discharge capacity in the cell by having the first load condition removed from the cell at a first time so that the cell'"'"'s discharge voltage relaxes from a first voltage at the first load to a second voltage at a second, lighter load or at an open circuit voltage condition and wherein the voltage change from the first voltage to the second voltage is measurable and wherein the time interval for the cell to relax from the first voltage at the first time to the second voltage at the second time is measurable and wherein the voltage change is divisible by the time interval to determine a Δ

OCV/Δ

Hrs ratio and wherein the depth-of-discharge ratio for the cell is then determinable using the equation;

DOD=e<sup>[−

5.00−

2.44 ln(Δ

OCV/Δ

Hrs)]</sup>.

2. The combination of claim 1 wherein the solid cathode comprises fluorinated carbon as an active material.

3. The combination of claim 1 wherein the solid cathode is selected from the group consisting of silver vanadium oxide, copper silver vanadium oxide, manganese dioxide, cobalt oxide, nickel oxide, fluorinated carbon, copper oxide, copper sulfide, iron sulfide, iron disulfide, titanium disulfide and copper vanadium oxide, and mixtures thereof.

4. The combination of claim 1 wherein the cathode comprises from about 80 to about 99 weight percent of a cathode active material.

5. The combination of claim 1 wherein the cathode further comprises a binder material and a conductive additive.

6. The combination of claim 5 wherein the binder material is a fluoro-resin powder.

7. The combination of claim 5 wherein the conductive additive is selected from the group consisting of carbon, graphite powder, acetylene black and metallic powder selected from the group consisting of titanium, aluminum, nickel and stainless steel, and mixtures thereof.

8. The combination of claim 1 wherein the cathode comprises from about 0 to 3 weight percent carbon, about 1 to 5 weight percent of a powder fluoro-resin and about 94 weight percent of the cathode active material.

9. The combination of claim 1 wherein the cell is activated with the nonaqueous electrolyte having an inorganic salt dissolved therein, wherein the alkali metal of the salt is the same as the alkali metal comprising the anode.

10. The combination of claim 9 wherein the nonaqueous solvent from the group consisting of tetrahydrofuran, methyl acetate, diglyme, triglyme, tetraglyme, 1,2-dimethoxyethane, 1,2-diethoxyethane, 1-ethoxy, 2-methoxyethane, dimethyl carbonate, diethyl carbonate, dipropyl carbonate, ethyl methyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, propylene carbonate, ethylene carbonate, butylene carbonate, acetonitrile, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, γ

-valerolactone, γ

-butyrolactone and N-methyl-pyrrolidinone, and mixtures thereof.

11. The combination of claim 9 wherein the alkali metal salt is selected from the group consisting of LiPF₆, LiBF₄, LiAsF₆, LiSbF₆, LiClO₄, LiAlCl₄, LiGaCl₄, LiC(SO₂CF₃)₃, LiN(SO₂CF₃)₂, LiSCN, LiO₂, LiO₃SCF₂CF₃, LiC₆F₅SO₃, LiO₂CCF₃, LiSO₃F, LiB(C₆H₅)₄ and LiCF₃SO₃, and mixtures thereof.

12. The combination of claim 1 wherein the cell has a lithium anode active material in electrical contact with a nickel current collector and the cathode comprises fluorinated carbon active material in electrical contact with a titanium current collector and wherein the anode and the cathode are activated with the electrolyte solution comprising 1.0M LIBF₄ in γ

-butyrolactone.

13. A method for determining the remaining discharge capacity in an electrochemical cell, comprising the steps of:

a) providing the electrochemical cell comprising a lithium anode and a fluorinated carbon cathode activated with a nonaqueous electrolyte;

b) determining a stoichiometric capacity of the cell;

c) discharging the cell under a first load condition;

d) removing the first load from the cell at a first time so that the cell'"'"'s discharge voltage relaxes from a first voltage at the first load to a second voltage at a second, lighter load or at an open circuit voltage condition and measuring the voltage change from the first voltage to the second voltage;

e) measuring the time interval for the cell to relax from the first voltage at the first time to the second voltage at the second time;

f) dividing the voltage change by the time interval to determine Δ

OCV/Δ

Hrs ratio; and

g) computing the depth of discharge equaling e<sup>[−

5.00−

2.44 ln(Δ

OCV/Δ

Hrs)]</sup>.

14. The method of claim 13 including providing the solid cathode having fluorinated carbon as an active material.

15. The method of claim 13 including selecting the solid cathode from the group consisting of silver vanadium oxide, copper silver vanadium oxide, manganese dioxide, cobalt oxide, nickel oxide, fluorinated carbon, copper oxide, copper sulfide, iron sulfide, iron disulfide, titanium disulfide and copper vanadium oxide, and mixtures thereof.

16. The method of claim 13 including providing the cathode comprising from about 80 to about 99 weight percent of a cathode active material.

17. The method of claim 13 including providing the cathode further comprising a binder material and a conductive additive.

18. The method of claim 17 wherein the binder material is a fluoro-resin powder.

19. The method of claim 17 including selecting the conductive additive from the group consisting of carbon, graphite powder, acetylene black and metallic powder selected from the group consisting of titanium, aluminum, nickel and stainless steel, and mixtures thereof.

20. The method of claim 13 wherein the cathode comprises from about 0 to 3 weight percent carbon, about 1 to 5 weight percent of a powder fluoro-resin and about 94 weight percent of the cathode active material.

21. The method of claim 13 including activating the cell with the nonaqueous electrolyte having an inorganic salt dissolved therein, wherein the alkali metal of the salt is the same as the alkali metal comprising the anode.

22. The method of claim 21 including selecting the nonaqueous solvent from the group consisting of tetrahydrofuran, methyl acetate, diglyme, triglyme, tetraglyme, 1,2-dimethoxyethane, 1,2-diethoxyethane, 1-ethoxy, 2-methoxyethane, dimethyl carbonate, diethyl carbonate, dipropyl carbonate, ethyl methyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, propylene carbonate, ethylene carbonate, butylene carbonate, acetonitrile, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, γ

-valerolactone, γ

-butyrolactone and N-methyl-pyrrolidinone, and mixtures thereof.

23. The method of claim 21 including selecting the alkali metal salt from the group consisting of LiPF₆, LiBF₄, LiAsF₆, LiSbF₆, LiClO₄, LiAlCl₄, LiGaCl₄, LiC(SO₂CF₃)₃, LiN(SO₂CF₃)₂, LiSCN, LiO₂, LiO₃SCF₂CF₃, LiC₆F₅SO₃, LiO₂CCF₃, LiSO₃F, LiB(C₆H₅)₄ and LiCF₃SO₃, and mixtures thereof.

24. The method of claim 13 including providing the cell having lithium anode active material in electrical contact with a nickel current collector and the cathode comprises fluorinated carbon active material in electrical contact with a titanium current collector and wherein the anode and the cathode are activated with the electrolyte solution comprising 1.0M LiBF₄ in γ

-butyrolactone.

25. The method of claim 13 including providing the cell powering an implantable medical device.

26. A method for determining the remaining discharge capacity in an electrochemical cell, comprising the steps of:

a) providing an electronic device powered by the electrochemical cell;

b) providing the electrochemical cell comprising a lithium anode and a fluorinated carbon cathode activated with a nonaqueous electrolyte;

c) determining a stoichiometric capacity of the cell;

d) discharging the cell under a first load condition;

e) removing the first load from the cell at a first time so that the cell'"'"'s discharge voltage relaxes from a first voltage at the first load to a second voltage at a second, lighter load or at an open circuit voltage condition and measuring the voltage change from the first voltage to the second voltage;

f) measuring the time interval for the cell to relax from the first voltage at the first time to the second voltage at the second time;

g) dividing the voltage change by the time interval to determine a Δ

OCV/Δ

Hrs ratio; and

h) computing the depth of discharge equaling e<sup>[−

5.00−

2.44 ln(Δ

OCV/Δ

Hrs)]</sup>.