Nickel-zinc battery

Patent metadata

Field	Value
Publication number	US-2017104241-A1
Application number	US-201615386212-A
Country	US
Kind code	A1
Filing date	Dec 21, 2016
Priority date	Jul 9, 2014
Publication date	Apr 13, 2017
Grant date	—

Abstract

Provided is a highly reliable nickel-zinc battery including a separator exhibiting hydroxide ion conductivity and water impermeability. The separator is disposed in a hermetic container to separate a positive-electrode chamber accommodating a positive electrode and a positive-electrode electrolyte from a negative-electrode chamber accommodating a negative electrode and a negative-electrode electrolyte. 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 meeting a variation in amount of water in association with reaction at the negative electrode during charge and discharge of the battery. The nickel-zinc battery further includes a gas flow channel that connects the extra positive-electrode space to the extra negative-electrode space such that the spaces are in gas communication with each other.

First claim

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 wherein the nickel-zinc battery further comprises a gas flow channel that connects the extra positive-electrode space to the extra negative-electrode space such that the spaces are in gas communication with each other.

2 . The nickel-zinc battery according to claim 1 , wherein the gas flow channel is disposed so as to establish a connection between a portion of the positive-electrode chamber located at a position which the positive-electrode electrolytic solution does not reach even after an increase in amount of water through charging and a portion of the negative-electrode chamber located at a position which the negative-electrode electrolytic solution does not reach even after an increase in amount of water through discharging.

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 3 , wherein the gas flow channel is disposed so as to connect the top of the positive-electrode chamber or the vicinity of the top of the positive-electrode chamber to the top of the negative-electrode chamber or the vicinity of the top of the negative-electrode chamber.

5 . The nickel-zinc battery according to claim 1 , wherein the gas flow channel is disposed such that neither the positive-electrode electrolytic solution nor the negative-electrode electrolytic solution passes therethrough.

6 . The nickel-zinc battery according to claim 1 , 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.

7 . The nickel-zinc battery according to claim 1 , 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.

8 . 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.

9 . The nickel-zinc battery according to claim 1 , wherein the separator comprises an inorganic solid electrolyte.

10 . The nickel-zinc battery according to claim 9 , wherein the inorganic solid electrolyte has a relative density of 90% or more.

11 . The nickel-zinc battery according to claim 9 , wherein the inorganic solid electrolyte comprises a layered double hydroxide.

12 . The nickel-zinc battery according to claim 11 , wherein the layered double hydroxide has 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 at least one divalent cation, M 3+ represents at least one 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.

13 . The nickel-zinc battery according to claim 9 , wherein the inorganic solid electrolyte is in a plate, membrane, or layer form.

14 . The nickel-zinc battery according to claim 1 , further comprising a porous substrate on either or both of the surfaces of the separator.

15 . The nickel-zinc battery according to claim 14 , wherein the inorganic solid electrolyte is in a membrane or layer form, and is disposed on or in the porous substrate.

16 . The nickel-zinc battery according to claim 9 , wherein the inorganic solid electrolyte is densified through hydrothermal treatment.

17 . The nickel-zinc battery according to claim 1 , wherein the alkali metal hydroxide is potassium hydroxide.

18 . 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.

19 . The nickel-zinc battery according to claim 14 , wherein the inorganic solid electrolyte comprises a layered double hydroxide, wherein the layered double hydroxide is composed of an aggregation of platy particles, and wherein the platy particles are oriented such that tabular faces of the platy particles are perpendicular to or oblique to the surface of the porous substrate.

20 . The nickel-zinc battery according to claim 14 , wherein the porous substrate is composed of a polymer, and the polymer is at least one selected from the group consisting of polystyrene, polyether sulfone, polypropylene, epoxy resin, and polyphenylene sulfide.

Assignees

• Ngk Insulators Ltd

Inventors

• Hayashi Hiroshi
• Yamada Naohito
• Kitoh Kenshin

Classifications

• H01M10/28

  Construction or manufacture · CPC title

• H01M4/244

  Zinc electrodes · CPC title

• H01M2300/0014

  Alkaline electrolytes · CPC title

• H01M10/34

  Gastight accumulators · CPC title

• H01M10/26

  Selection of materials as electrolytes · CPC title