Thin film battery device and method of formation
US-2017301955-A1 · Oct 19, 2017 · US
US10141545B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10141545-B2 |
| Application number | US-201615073706-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 18, 2016 |
| Priority date | Dec 29, 2010 |
| Publication date | Nov 27, 2018 |
| Grant date | Nov 27, 2018 |
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Bead blasting the inner, contact surface of an electrochemical cell casing to render the inner surface thereof essentially contamination free and suitable as a current collector is described. The casing is preferably of stainless steel and houses the alkali metal-halogen couple in a case-positive configuration.
Opening claim text (preview).
What is claimed is: 1. An electrochemical cell, comprising: a) a casing of an electrically conductive material; b) a lithium anode supported on an anode current collector housed inside the casing; c) a glass-to-metal seal supported by the casing and configured to electrically isolate the anode current collector from the casing; and d) a cathode comprising an iodine-containing material in electrochemical association with the lithium anode inside the casing, wherein the iodine-containing material contacts an inner surface of the casing serving as a cathode current collector, e) wherein, prior to contact with the iodine-containing material, at least a portion of the inner surface of the casing is characterized as having been subjected to a pressurized stream of beads, f) wherein the cell has a rate capacity of about 1.32 Ah, and g) wherein, after fabrication, the cell is characterized as having been discharged at 37° C. under a 6.98K load for a period of about 60 hours, followed by having been subjected to a 100K load for about 24 hours so that the cell exhibits a final 100K loaded voltage of about 2,724 mV±3 mV and a final 100K loaded impedance of 90±5 ohms. 2. The electrochemical cell of claim 1 , configured to discharge according to the following reaction: 2Li+I 2 →LiI, and having an open circuit voltage of from about 2.7 to 2.8 volts. 3. The electrochemical cell of claim 1 , wherein the cathode comprises a mixture of iodine and carbon or graphite. 4. The electrochemical cell of claim 1 , wherein the iodine-containing material is characterized as having been filled into the casing as a flowable substance. 5. The electrochemical cell of claim 1 , wherein the casing comprises an electrically conductive material selected from the group consisting of stainless steel, titanium, mild steel, nickel plated steel, aluminum, and nickel cobalt alloys. 6. The electrochemical cell of claim 1 , wherein the glass-to-metal seal is supported in a lid comprising the casing. 7. The electrochemical cell of claim 1 , wherein the inner surface of the casing is characterized as having been subjected to the pressurized stream of beads from about 2 seconds to about 10 seconds. 8. The electrochemical cell of claim 1 , wherein, prior to contact with the iodine-containing material, at least the portion of the inner surface of the casing is characterized as having been subjected to the pressurized stream of beads for about 2 to about 10 seconds. 9. The electrochemical cell of claim 1 , wherein, prior to contact with the iodine-containing material, at least the portion of the inner surface of the casing is characterized as having been subjected to the pressurized stream of beads at a pressure from about 0.34 MPa (50 psi) to about 0.48 MPa (70 psi). 10. The electrochemical cell of claim 1 , wherein, prior to contact with the iodine-containing material, at least the portion of the inner surface of the casing is characterized as having been subjected to the pressurized stream of beads selected from the group consisting of metal beads, alumina beads, and glass beads. 11. The electrochemical cell of claim 10 , wherein the glass beads have a grain size from about 35 μm to about 65 μm, per MIL SPEC “G”-9954A. 12. The electrochemical cell of claim 1 , wherein the cathode comprises a charge transfer complex and iodine. 13. The electrochemical cell of claim 12 , wherein the charge transfer complex is selected from the group consisting of pyrene, perylene, anthracene, naphthalene, erythrosine, azulene, fluorene, polyethylene, polypropylene, polystyrene, polypyrrole, polyamides, polyvinyls, phenothiazine, phenazine, 10-phenylphenophiozine, thianthrene, 10-methylthiazinc, methalyineblue, poly-2-vinyl quinoline, poly-2-vinyl pyridine, poly-4-vinyl pyridine, poly-5-vinyl-2-methyl-pyridine, poly-N-vinyl carbazole. 14. The electrochemical cell of claim 12 , wherein the charge transfer complex comprises an organic donor component and an electron acceptor. 15. The electrochemical cell of claim 14 , wherein the electron acceptor has a conductivity greater than about 2.5×10 −4 ohm/cm. 16. An electrochemical cell, comprising: a) a casing of stainless steel; b) a lithium anode supported on an anode current collector comprised of nickel, the lithium anode being housed inside the casing; c) a glass-to-metal seal supported by the casing, wherein the glass-to-metal seal is configured to electrically isolate the anode current collector from the casing; and d) a cathode comprising an iodine-containing material in electrochemical association with the lithium anode inside the casing, wherein the iodine-containing material contacts an inner surface of the casing serving as a cathode current collector, e) wherein, prior to contact with the iodine-containing material, at least a portion of the inner surface of the casing is characterized as having been subjected to a pressurized stream of beads, and f) wherein, after fabrication, the cell is characterized as having been discharged at 37° C. under a 6.98K load for a period of about 60 hours, followed by having been subjected to a 100K load for about 24 hours so that the cell exhibits a final 100K loaded voltage of about 2,724 mV±3 mV and a final 100K loaded impedance of 90±5 ohms. 17. The electrochemical cell of claim 16 having a rate capacity of 1.32 Ah. 18. An electrochemical cell, comprising: a) a casing of stainless steel; b) a lithium anode supported on an anode current collector comprised of nickel, the lithium anode being housed inside the casing; c) a glass-to-metal seal supported by the casing, wherein the glass-to-metal seal is configured to electrically isolate the anode current collector from the casing; and d) a cathode comprising an iodine-containing material in electrochemical association with the lithium anode inside the casing, wherein the iodine-containing material contacts an inner surface of the casing serving as a cathode current collector, e) wherein, prior to contact with the iodine-containing material, at least a portion of the inner surface of the casing is characterized as having been subjected to a pressurized stream of glass beads having a grain size from about 35 μm to about 65 μm, per MIL SPEC “G”-9954A at a pressure from about 0.34 MPa (50 psi) to about 0.48 MPa (70 psi), and f) wherein, after fabrication, the cell is characterized as having been discharged at 37° C. under a 6.98K load for a period of about 60 hours, followed by having been subjected to a 100K load for about 24 hours so that the cell exhibits a final 100K loaded voltage of about 2,724 mV±3 mV and a final 100K loaded impedance of 90±5 ohms. 19. The electrochemical cell of claim 18 having a rate capacity of 1.32 Ah.
Devices for making primary cells · CPC title
having curved cross-section, e.g. round or elliptic (H01M50/103, H01M50/109, H01M50/11 take precedence) · CPC title
Metals · CPC title
Electricity · mapped topic
Lithium (H01M4/405 takes precedence) · CPC title
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