Secondary Battery Module
US-2024297362-A1 · Sep 5, 2024 · US
US10381689B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10381689-B2 |
| Application number | US-201615177591-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 9, 2016 |
| Priority date | Jul 9, 2014 |
| Publication date | Aug 13, 2019 |
| Grant date | Aug 13, 2019 |
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Provided is a highly reliable nickel-zinc battery including a separator exhibiting hydroxide ion conductivity and water impermeability. The nickel-zinc battery of the present invention includes a positive electrode containing nickel oxide and/or nickel oxyhydroxide; a positive-electrode electrolytic solution in which the positive electrode is immersed, the electrolytic solution containing an alkali metal hydroxide; a negative electrode containing zinc and/or zinc oxide; a negative-electrode electrolytic solution in which the negative electrode is immersed, the electrolytic solution containing an alkali metal hydroxide; a hermetic container accommodating the positive electrode, the positive-electrode electrolytic solution, the negative electrode, and the negative-electrode electrolytic solution; and the separator exhibiting hydroxide ion conductivity and water impermeability and disposed in the hermetic container so as to separate a positive-electrode chamber accommodating the positive electrode and the positive-electrode electrolytic solution from a negative-electrode chamber accommodating the negative electrode and the negative-electrode electrolytic solution.
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What is claimed is: 1. A nickel-zinc battery comprising: a positive electrode comprising nickel hydroxide and/or nickel oxyhydroxide; a positive-electrode electrolytic solution comprising an alkali metal hydroxide, the positive electrode being immersed in the positive-electrode electrolytic solution; a negative electrode comprising zinc and/or zinc oxide; a negative-electrode electrolytic solution comprising an alkali metal hydroxide, the negative electrode being immersed in the negative-electrode electrolytic solution; a hermetic container accommodating the positive electrode, the positive-electrode electrolytic solution, the negative electrode, and the negative-electrode electrolytic solution; and a separator exhibiting hydroxide ion conductivity and water impermeability, the separator being disposed in the hermetic container so as to separate a positive-electrode chamber accommodating the positive electrode and the positive-electrode electrolytic solution from a negative-electrode chamber accommodating the negative electrode and the negative-electrode electrolytic solution, wherein the positive-electrode chamber has an extra positive-electrode space having a volume that meets a variation in amount of water in association with reaction at the positive electrode during charge and discharge of the battery, and the negative-electrode chamber has an extra negative-electrode space having a volume that meets a variation in amount of water in association with reaction at the negative electrode during charge and discharge of the battery, and (i) wherein the extra positive-electrode space has a volume greater than the amount of water that will increase in association with reaction at the positive electrode during the charge of the battery; the extra positive-electrode space is not preliminarily filled with the positive-electrode electrolytic solution; the extra negative-electrode space has a volume greater than the amount of water that will decrease in association with reaction at the negative electrode during the charge of the battery; and the extra negative-electrode space is preliminarily filled with an amount of the negative-electrode electrolytic solution that will decrease during the charge of the battery; or (ii) wherein the extra positive-electrode space has a volume greater than the amount of water that will decrease in association with reaction at the positive electrode during the discharge of the battery; the extra positive-electrode space is preliminarily filled with an amount of the positive-electrode electrolytic solution that will decrease during the discharge of the battery; the extra negative-electrode space has a volume greater than the amount of water that will increase in association with reaction at the negative electrode during the discharge of the battery; and the extra negative-electrode space is not preliminarily filled with the negative-electrode electrolytic solution. 2. The nickel-zinc battery according to claim 1 , wherein the extra positive-electrode space is not filled with the positive electrode and/or the extra negative-electrode space is not filled with the negative electrode. 3. The nickel-zinc battery according to claim 1 , wherein the separator is vertically disposed, the extra positive-electrode space is provided in an upper portion of the positive-electrode chamber, and the extra negative-electrode space is provided in an upper portion of the negative-electrode chamber. 4. The nickel-zinc battery according to claim 1 , wherein the separator comprises an inorganic solid electrolyte. 5. The nickel-zinc battery according to claim 4 , wherein the inorganic solid electrolyte has a relative density of 90% or more. 6. The nickel-zinc battery according to claim 4 , wherein the inorganic solid electrolyte comprises a layered double hydroxide having a basic composition represented by the formula: M 2+ 1−x M 3+ x (OH) 2 A n− x/n · m H 2 O where M 2+ represents a divalent cation, M 3+ represents a trivalent cation, A n− represents an n-valent anion, n is an integer of 1 or more, x is 0.1 to 0.4, and m is any real number. 7. The nickel-zinc battery according to claim 5 , wherein M 2+ comprises Mg 2+ , M 3+ comprises Al 3+ , and A − comprises OH − and/or CO 3 2− in the formula. 8. The nickel-zinc battery according to claim 4 , wherein the inorganic solid electrolyte is in a plate, membrane, or layer form. 9. The nickel-zinc battery according to claim 1 , further comprising a porous substrate on either or both of the surfaces of the separator. 10. The nickel-zinc battery according to claim 9 , wherein the inorganic solid electrolyte is in a membrane or layer form, and is disposed on or in the porous substrate. 11. The nickel-zinc battery according to claim 4 , wherein the inorganic solid electrolyte is densified through hydrothermal treatment. 12. The nickel-zinc battery according to claim 1 , wherein the alkali metal hydroxide is potassium hydroxide. 13. The nickel-zinc battery according to claim 1 , further comprising a positive-electrode collector in contact with the positive electrode, and a negative-electrode collector in contact with the negative electrode.
inorganic · CPC title
Alkaline electrolytes · CPC title
Gastight accumulators · CPC title
Nickel accumulators (H01M10/34 takes precedence) · CPC title
Alloys based on zinc · CPC title
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