1.5-3 V lithium batteries with overcharge protection
Rechargeable, non-aqueous lithium batteries which contain, as active anode material, either lithium metal or a lithium alloy, an active cathode material with a redox potential in the range of between 1.5 and 3.4 V vs Li/Li + and lithium rhodanide (LiSCN) as electrolyte component. One or more related methods for providing overcharge protection are also described herein.
1. A method for providing overcharge protection to a rechargeabe and non-aqueous lithium battery, the method comprising:
providing the rechargeabe and non-aqueous lithium battery comprising an anode comprising active anode material, a cathode comprising an active cathode material having a redox potential in a range from about 1.5 and 3.4 V vs. Li/Li + , and an electrolyte comprising at east one additional conductive salt and a redox shuttle compound present in the electrolyte in a concentration in a range from 0.01 to 15 wt. %,
wherein the redox shuttle is lithium rhodanide (LiSCN),
wherein the at least one additional conductive salt is selected from the group consisting of LiPF 6 , a lithium fluoroalkyl phosphate, LiBF 4 , LiOSO 2 CF 3 , a methide salt, LiClO 4 , a lithium chelatoborate, a lithium fluorochelatoborate, a lithium chelatophosphate, a lithium fluorochelatophosphate and a lithium halide;
charging the rechargeabe and non-aqueous lithium battery at a charging voltage greater than the redox potential of the active cathode material,
wherein the charging voltage is about 0.5 to 1.5 V above the redox potential of the active cathode material.
2. The method of claim 1 wherein the rechargeable and non-aqueous lithium battery is not used with a battery management system during charging.
3. The method of claim 1 , wherein the active anode material is selected from the group consisting of lithium metal and a lithium alloy.
4. The method of claim 1 , wherein the active anode material is a powder and present in a compacted form as the active anode material.
5. The method of claim 1 , wherein the active cathode material is selected from the group consisting of CF x , MnO 2 , V 2 O 5 , V 6 O 13 , FeOF, FeF 3 , S, and FeF 2 .
6. The method of claim 1 , wherein the electrolyte is in a liquid, gelatinous or solid state at room temperature.
7. The method of claim 1 , wherein the electrolyte comprises organic aprotic solvents selected from the group consisting of a cyclic ether, an acyclic ether, a polyether, a nitrile, a lactone, a carbonic acid ester and an ionic liquid.
8. The method of claim 1 , wherein the electrolyte comprises at least one organic aprotic solvent selected from the group consisting of tetrahydropyran, tetrahydrofuran, 1,2-dimethoxyethane, diethylene glycol dimethyl ether, acetonitrile, adiponitrile, malodinitrile, glutaronitrile, γ-butyrolactone and an imidazolium salt.
9. The method of claim 1 , wherein the electrolyte further comprises at least one organic polymer selected from the group consisting of polyethylene oxide, polyacrylonitrile, polyvinylidene fluoride, and any combination of two or more of the foregoing.
10. The method of claim 1 further comprising:
oxidizing the redox shuttle compound to form an oxidized redox shuttle compound;
diffusing the oxidized redox shuttle compound to the anode; and
discharging the oxidized redox shuttle compound to form the redox shuttle compound.
11. The method of claim 1 , wherein the redox shuttle compound is present in the electrolyte in a concentration in the range of from 0.01 to 10 wt. %.
12. The method of claim 11 , wherein the active cathode material is selected from the group consisting of CF x , a transition metal oxide, a transition metal sulfide, a transition metal fluoride, a transition metal oxyfluoride, an organic redox-active compound, sulfur, and selenium.
13. A method for providing overcharge protection to a rechargeabe and non-aqueous lithium battery, the method comprising:
providing the rechargeabe and non-aqueous lithium battery comprising an anode comprising active anode material, a cathode comprising an active cathode material having a redox potential in a range from about 1.5 and 3.4 V vs. Li/Li + , and an electrolyte comprising at least one additional conductive salt and a redox shuttle compound present in the electrolyte in a concentration in a range from 0.01 to 15 wt. %,
wherein the redox shuttle is lithium rhodanide (LiSCN), and
the active cathode material is selected from the group consisting of CF x , MnO 2 , V 2 O 5 V 6 O 13 , FeOF, FeF 3 , S, and FeF 2 ,
wherein the at last one additional conductive salt is selected from the group consisting of LiPF 6 , a lithium fluoroalkyl phosphate, LiBF 4 , LiOSO 2 CF 3 , a methide salt, LiClO 4 , a lithium chelatoborate, a lithium fluorochelatoborate, a lithium chelatophosphate, a lithium fluorochelatophosphate and a lithium halide; and
charging the rechargeabe and non-aqueous lithium battery at a charging voltage greater than the redox potential of the active cathode material,
wherein the charging voltage is about 0.5 to 1.5 V above the redox potential of the active cathode material;
oxidizing the redox shuttle compound to form an oxidized redox shuttle compound;
diffusing the oxidized redox shuttle compound to the anode; and
discharging the oxidized redox shuttle compound to form the redox shuttle compound.
14. The method of claim 13 wherein the rechargeable and non-aqueous lithium battery is not used with a battery management system during charging.
15. The method of claim 13 , wherein the electrolyte further comprises at least one organic aprotic solvent selected from the group consisting of tetrahydropyran, tetrahydrofuran, 1,2-dimethoxyethane, diethylene glycol dimethyl ether, acetonitrile, adiponitrile, malodinitrile, glutaronitrile, y-butyrolactone and an imidazolium salt.