Control of silver vanadium oxide surface areas as a means of controlling voltage delay and Rdc growth in an electrochemical cell
An electrochemical cell comprising a lithium anode, a cathode comprising a blank cut from a free-standing sheet of a silver vanadium oxide mixture contacted to a current collector. The active material has having a relatively lower surface area and an electrolyte activating the anode and the cathode is described. By optimizing the cathode active material surface area in a SVO-containing cell, the magnitude of the passivating film growth at the solid-electrolyte interphase (SEI) and its relative impermeability to lithium ion diffusion is reduced. Therefore, by using a cathode of an active material in a range of from about 0.2 m 2 /gram to about 2.6 m 2 /gram, and preferably from about 1.6 m 2 /gram to about 2.4 m 2 /gram, it is possible to eliminate or significantly reduce undesirable irreversible Rdc growth and voltage delay in the cell and to extend its useful life in an implantable medical device.
1. An electrochemical cell, which comprises:
a) a lithium anode;
b) a cathode comprising silver vanadium oxide (SVO) as a cathode active material, wherein the SVO has a surface area from about 1.6 m 2 /g to about 1.9 m 2 /gram; and
c) an electrolyte activating the anode and the cathode.
2. The electrochemical cell of claim 1 wherein the cathode has a configuration selected from the group consisting of: SVO/current collector/CF x /current collector/SVO, SVO/current collector/SVO/CF/SVO/current collector/SVO, and SVO/current collector/CF x , with the SVO facing the lithium anode.
3. The electrochemical cell of claim 1 wherein the cathode comprises from between about 80 weight percent to about 98 weight percent of the cathode active material.
4. The electrochemical cell of claim 1 wherein the cathode further comprises a conductive additive.
5. The electrochemical cell of claim 1 wherein the cathode further comprises a fluoro-polymer binder material selected from powdered polytetrafluoroethylene and powdered polyvinylidene fluoride present at about 1 to about 5 weight percent of the cathode mixture.
6. The electrochemical cell of claim 1 wherein the cathode is comprised of a current collector selected from the group consisting of stainless steel, titanium, tantalum, platinum, gold, aluminum, cobalt nickel alloys, highly alloyed ferritic stainless steel containing molybdenum and chromium, and nickel-, chromium-, and molybdenum-containing alloys.
7. The electrochemical cell of claim 1 wherein the electrolyte has a first solvent selected from the group consisting of tetrahydrofuran, methyl acetate, diglyme, trigylme, tetragylme, dimethyl carbonate, 1,2-dimethoxyethane, 1,2-diethoxyethane, 1-ethoxy,2-methoxyethane, ethyl methyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, diethyl carbonate, dipropyl carbonate, and mixtures thereof, and a second solvent selected from the group consisting of propylene carbonate, ethylene carbonate, butylene carbonate, acetonitrile, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, γ-valerolactone, γ-butyrolactone, N-methyl-pyrrolidinone, and mixtures thereof.
8. The electrochemical cell of claim 1 wherein the electrolyte includes a lithium salt selected from the group consisting of LiPF 6 , LiEF 4 , LiAsF 6 , LiSbF 6 , LiClO 4 , LiO 2 , LiAlCl 4 , LiGaCl 4 , LiC(SO 2 CF 3 ) 3 , LiN(SO 2 CF 3 ) 2 , LiSCN, LiO 3 SCF 3 , LiC 6 F 5 SO 3 , LiO 2 CCF 3 , LiSO 6 F, LiB(C 6 H 5 ) 4 , LiCF 3 SO 3 , and mixtures thereof.
9. The electrochemical cell of claim 1 wherein the electrolyte is 0.8M to 1.5M LiAsF 6 or LiPF 6 dissolved in a 50:50 mixture, by volume, of propylene carbonate and 1,2-dimethoxyethane.
10. A method for providing an electrochemical cell, comprising the steps of
a) providing an anode;
b) providing a cathode comprising silver vanadium oxide (SVO) a cathode active material, wherein the SVO has a surface area from about 1.6 m 2 /gram to about 1.9 m 2 /g;
c) positioning the anode and the cathode inside a casing with an intermediate separator preventing direct physical contact between them; and
d) activating the anode and the cathode with an electrolyte.
11. The method of claim 10 including providing the cathode having a configuration selected from the group consisting of: SVO/current collector/CF x /current collector/SVO, SVO/current collector/SVO/CF x /SVO/current collector/SVO, and SVO/current collector/CF x , with the SVO facing the lithium anode.
12. An electrochemical cell, which comprises:
a) a lithium anode;
b) a cathode comprising silver vanadium oxide (SVO) as a cathode active material having the formula Ag x V 2 O y and being selected from the phases consisting of β-phase silver vanadium oxide having in the general formula x=0.35 and y=5.8, γ-phase silver vanadium oxide having in the general formula x=0.80 and y=5.40 and ε-phase silver vanadium oxide having in the general formula x=1.0 and y=5.5, and combinations and mixtures of phases thereof, wherein the silver vanadium oxide has a surface area from about 1.6 m 2 /gram to about 1.9 m 2 /g; and
c) an electrolyte activating the anode and the cathode.
13. The electrochemical cell of claim 12 wherein the cathode has a configuration selected from the group consisting of: SVO/current collector/CF x /current collector/SVO, SVO/current collector/SVO/CF x /SVO/current collector/SVO, and SVO/current collector/CF x , with the SVO facing the lithium anode.
14. The electrochemical cell of claim 12 wherein the cathode comprises from between about 80 weight percent to about 98 weight percent of the cathode active material.
15. The electrochemical cell of claim 12 wherein the cathode further comprises a conductive additive.
16. The electrochemical cell of claim 12 wherein the cathode further comprises a fluoro-polymer binder material selected from powdered polytetrafluoroethylene and powdered polyvinylidene fluoride present at about 1 to about 5 weight percent of the cathode mixture.
17. The electrochemical cell of claim 12 wherein the cathode is comprised of a current collector selected from the group consisting of stainless steel, titanium, tantalum, platinum, gold, aluminum, cobalt nickel alloys, highly alloyed ferritic stainless steel containing molybdenum and chromium, and nickel-, chromium-, and molybdenum-containing alloys.
18. The electrochemical cell of claim 12 wherein the electrolyte has a first solvent selected from the group consisting of tetrahydrofuran, methyl acetate, diglyme, trigylme, tetragylme, dimethyl carbonate, 1,2-dimethoxyethane, 1,2-diethoxyethane, 1-ethoxy,2-methoxyethane, ethyl methyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, diethyl carbonate, dipropyl carbonate, and mixtures thereof, and a second solvent selected from the group consisting of propylene carbonate, ethylene carbonate, butylene carbonate, acetonitrile, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, γ-valerolactone, γ-butyrolactone, N-methyl-pyrrolidinone, and mixtures thereof.
19. The electrochemical cell of claim 12 wherein the electrolyte includes a lithium salt selected from the group consisting of LiPF 6 , LiBF 4 , LiAsF 6 , LiSbF 6 , LiClO 4 , LiO 2 , LiAlCl 4 , LiGaCl 4 , LiC(SO 2 CF 3 ) 3 , LiN(SO 2 CF 3 ) 2 , LiSCN, LiO 3 SCF 3 , LiC 6 F 5 SO 3 , LiO 2 CCF 3 , LiSO 6 F, LiB(C 6 H 5 ) 4 , LiCF 3 SO 3 , and mixtures thereof.
20. The electrochemical cell of claim 12 wherein the electrolyte is 0.8M to 1.5M LiAsF 6 or LiPF 6 dissolved in a 50:50 mixture, by volume, of propylene carbonate and 1,2-dimethoxyethane.