JP7643238B2 - Negative electrode current collector and battery - Google Patents

Description

This disclosure relates to negative electrode current collectors and battery technology.

Conventionally, a technique has been known for forming an alloy layer between a base layer made of copper and a plating layer made of tin, which is formed on the base layer, in a negative electrode current collector by firing the base layer and the plating layer, which is made of tin. (Patent Document 1) In this technique, the alloy layer is a compound made of copper and tin.

Special Publication No. 2010-541183

In a battery equipped with a negative electrode including a negative electrode current collector and a negative electrode active material arranged around the negative electrode current collector, hydrogen may be generated at the negative electrode when an aqueous electrolyte is used. In this case, the generated hydrogen may adhere to the outer surface of the negative electrode, which may reduce the function of the battery. Therefore, a technology is desired that suppresses hydrogen generation at a negative electrode equipped with a negative electrode current collector and adhesion of hydrogen to the outer surface of the negative electrode.

The present disclosure can be realized in the following forms.
According to one embodiment of the present disclosure, there is provided a negative electrode current collector for a battery using an electrolyte, the negative electrode current collector comprising: a base layer mainly made of a conductive metal; a barrier layer mainly made of a transition metal laminated on the base layer; an alloy layer made of the transition metal and tin laminated on the barrier layer; and a plating layer mainly made of tin laminated on the alloy layer, the barrier layer containing at least one of boron, aluminum, phosphorus, titanium, and cobalt as a different element different from the transition metal.
(2) According to another aspect of the present disclosure, there is provided a battery comprising: the anode current collector according to the above aspect, an anode including an anode active material, a cathode current collector, a cathode including a cathode active material, a separator separating the anode and the cathode, and an electrolyte solution contained in a region where the anode, the cathode, and the separator are arranged.

(1) According to one embodiment of the present disclosure, a negative electrode current collector for a battery using an electrolyte solution is provided. The negative electrode current collector includes a base layer mainly composed of a conductive metal, a barrier layer mainly composed of a transition metal laminated on the base layer, an alloy layer formed by alloying the transition metal and tin laminated on the barrier layer, and a plating layer mainly composed of tin laminated on the alloy layer. According to this embodiment, the negative electrode current collector includes a barrier layer mainly composed of a transition metal, an alloy layer formed by alloying the transition metal and tin, and a plating layer mainly composed of tin. This can suppress hydrogen generation in a negative electrode having a negative electrode current collector, and therefore hydrogen can be suppressed from adhering to the outer surface of the negative electrode. In addition, when hydrogen is generated in a negative electrode, hydrogen can be held in a layer such as an alloy layer located inside the outer surface of the negative electrode current collector. Therefore, hydrogen can be suppressed from adhering to the outer surface of the negative electrode. Therefore, hydrogen can be suppressed from being generated in a negative electrode having a negative electrode current collector, and the hydrogen can be adhered to the outer surface of the negative electrode, thereby suppressing a decrease in the function of the battery.
(2) In the above embodiment, the electrolyte may be an alkaline aqueous electrolyte. According to this embodiment, since the electrolyte is alkaline, more hydroxy ions are present in the electrolyte than when an acidic or neutral electrolyte is used. Electrons generated by the reaction between the hydroxy ions and the negative electrode active material flow to the positive electrode side, thereby realizing the discharge function of the battery. On the other hand, there may be a case where the electrons generated by the reaction between the hydroxy ions and the negative electrode active material do not flow to the positive electrode side, but contribute to the reduction reaction of water in the electrolyte, causing the water in the electrolyte to be oxidized and hydrogen to be generated at the negative electrode. Even in this case, the negative electrode current collector includes a barrier layer, an alloy layer, and a plating layer, so that the generated hydrogen can be held in a layer such as an alloy layer located inside the outer surface of the negative electrode current collector. Therefore, hydrogen generation at the negative electrode can be suppressed.
(3) In the above embodiment, the transition metal may be at least one of nickel, iron, chromium, zirconium, and lanthanum. According to this embodiment, when hydrogen is generated at the negative electrode, a barrier layer can be formed by a transition metal having an exchange current density related to the hydrogen generation reaction smaller than that of gold. Therefore, in this embodiment, the hydrogen generation reaction is less likely to occur at the negative electrode compared to a case where a barrier layer is formed by a transition metal having an exchange current density related to the hydrogen generation reaction larger than that of gold. In other words, a barrier layer can be formed by a transition metal that can suppress hydrogen generation at the negative electrode.
(4) In the above embodiment, the barrier layer may have a thickness of 2 μm or more and 10 μm or less. According to this embodiment, the underlayer can be covered with the barrier layer without any gaps. Therefore, the possibility that the underlayer is exposed on the barrier layer can be reduced. Therefore, the possibility that the metal contained in the underlayer diffuses to the outer surface side of the negative electrode current collector can be reduced.
(5) In the above embodiment, the thickness of the plating layer may be 2 μm or more and 5 μm or less. According to this embodiment, the alloy layer can be covered with the plating layer without any loss. Therefore, when hydrogen is generated in the negative electrode, the possibility that a layer such as the alloy layer having a function of retaining hydrogen is exposed on the outer surface of the negative electrode current collector can be reduced. Therefore, the generation of hydrogen in the negative electrode can be further suppressed.
(6) In the above embodiment, the barrier layer may contain at least one of boron, aluminum, phosphorus, titanium, and cobalt as a different element different from the transition metal. According to this embodiment, the barrier layer contains a different element, which can impart an additional function such as reducing the solubility of the negative electrode active material in the electrolyte.
(7) In the above embodiment, the plating layer may further contain at least one of indium and bismuth. According to this embodiment, the plating layer contains a metal whose exchange current density related to the hydrogen generation reaction is equal to or less than that of tin. This makes it possible to reduce the exchange current density of the plating layer related to the hydrogen generation reaction. Therefore, hydrogen generation at the negative electrode can be further suppressed.
(8) According to another embodiment of the present disclosure, a battery is provided. The battery includes the negative electrode current collector described in the above embodiment, a negative electrode including a negative electrode active material, a positive electrode current collector, a positive electrode including a positive electrode active material, a separator separating the negative electrode and the positive electrode, and an electrolyte solution accommodated in an area where the negative electrode, the positive electrode, and the separator are arranged. According to this embodiment, the negative electrode current collector constituting the battery includes a barrier layer mainly composed of a transition metal, an alloy layer in which a transition metal and tin are alloyed, and a plating layer mainly composed of tin. This makes it possible to suppress hydrogen generation in a negative electrode including a negative electrode current collector. In addition, when hydrogen is generated in the negative electrode, hydrogen can be held in a layer such as an alloy layer located on the inside of the outer surface of the negative electrode current collector. Therefore, it is possible to suppress hydrogen from adhering to the outer surface of the negative electrode. Therefore, it is possible to suppress the deterioration of the function of the battery due to hydrogen adhering to the outer surface of the negative electrode.
The present disclosure can be realized in various forms other than the above-mentioned negative electrode current collector and battery, for example, in the form of a method for manufacturing a negative electrode current collector, a method for controlling a battery including the negative electrode current collector, a computer program for implementing the control method, a non-transitory recording medium on which the computer program is recorded, etc.

FIG. 2 is a cross-sectional view illustrating the internal structure of the battery according to the embodiment. FIG. 2 is an enlarged view of a region of FIG. FIG. 13 shows the results of measurement by cyclic voltammetry using the produced negative electrode. FIG. 4 is a diagram showing the conditions of a cycle durability test. FIG. 13 is a graph showing the results of a cycle durability test.

A. Embodiments:
A-1. Battery configuration:
Fig. 1 is a schematic cross-sectional view showing an outline of the internal structure of a battery 1 according to this embodiment. Fig. 1 shows a view of the battery 1 cut along a plane along the longitudinal direction. In this embodiment, the battery 1 is a cylindrical nickel-zinc secondary battery in which a battery container body is sealed with an upper lid and a lower lid. The type and shape of the battery 1 are not limited to this. The battery 1 may be, for example, a nickel-cadmium storage battery. The shape of the battery 1 may be, for example, a laminated type, a rectangular type, or a pack type.

Battery 1 includes a negative electrode 2, a positive electrode 5, two separators C1 and C2, and an electrolyte 8. The negative electrode 2, the positive electrode 5, the two separators C1 and C2, and the electrolyte 8 are contained in the internal space of battery 1 surrounded by the battery container body, the upper lid, and the lower lid. The negative electrode 2, the positive electrode 5, and the separators C1 and C2 are immersed in the electrolyte 8 in the internal space of battery 1.

The negative electrode 2 includes a negative electrode collector 20 and a negative electrode active material 28. The negative electrode collector 20 is conductive. The negative electrode collector 20 is electrically connected to a negative electrode terminal (not shown). Details of the negative electrode collector 20 will be described later with reference to FIG. 2.

The negative electrode active material 28 contributes to the oxidation-reduction reaction in the negative electrode 2. In this embodiment, the negative electrode active material 28 is mainly composed of at least one of zinc (Zn) and zinc oxide. Specifically, at least one of zinc (Zn) as a simple substance and zinc oxide (ZnO) is used as the main component of the negative electrode active material 28. When the main component of the negative electrode active material 28 is zinc, for example, a zinc alloy containing zinc may be used. In this disclosure, "main component" means "a proportion greater than 50 mass%."

The negative electrode active material 28 may further include additives such as a thickener, a binder, and other inorganic substances. The thickener is, for example, a cellulose-based polymer such as carboxymethylcellulose (CMC). The binder is, for example, a fluorine-based resin such as polytetrafluoroethylene (PTFE). Note that the components and composition constituting the negative electrode active material 28 are not limited to these. The additives of the negative electrode active material 28 may also be components that have properties that enhance corrosion resistance, infiltration, conductivity, etc.

The positive electrode 5 includes a positive electrode collector 50 and a positive electrode active material 58. The positive electrode collector 50 is conductive. The positive electrode collector 50 is electrically connected to a positive electrode terminal (not shown). The positive electrode collector 50 is mainly composed of a conductive metal. The conductive metal used for the positive electrode collector 50 is, for example, aluminum (Al), an alloy mainly composed of aluminum, nickel (Ni), or titanium (Ti). In this embodiment, the positive electrode collector 50 is mainly composed of nickel. The positive electrode active material 58 may contain additives such as a thickener, a binder, or other inorganic substances, similar to the negative electrode active material 28.

The positive electrode active material 58 contributes to the oxidation-reduction reaction in the positive electrode 5. In this embodiment, the positive electrode active material 58 is mainly composed of nickel (Ni) or nickel hydroxide. The positive electrode active material 58 is, for example, nickel hydroxide (Ni(OH ₂ )).

The separators C1 and C2 separate the negative electrode 2 and the positive electrode 5. Specifically, the separators C1 and C2 are walls provided between the negative electrode 2 and the positive electrode 5 to prevent an internal short circuit caused by contact between the negative electrode 2 and the positive electrode 5. In this embodiment, the first separator C1 is disposed on the negative electrode 2 side, and the second separator C2 is disposed on the positive electrode 5 side. The separators C1 and C2 have insulating properties and allow the electrolyte 8 to pass through. The separators C1 and C2 are, for example, porous films formed of polyolefins such as polypropylene (PP) and polyethylene (PE). The separators C1 and C2 may further include nonwoven fabrics formed of chemical fibers. The chemical fibers are, for example, any of polypropylene fibers, cellulose fibers, polyvinyl alcohol (PVA) fibers, and ethylene vinyl acetate (EVA) fibers.

The electrolyte 8 is a liquid having electrical conductivity. The electrolyte 8 is composed of either an aqueous electrolyte such as an alkaline aqueous solution or a non-aqueous electrolyte containing an organic electrolyte such as a lithium salt. In this embodiment, the electrolyte 8 is an alkaline aqueous electrolyte. The alkaline aqueous electrolyte as the electrolyte 8 contains an alkali metal hydroxide and water. The electrolyte 8 is, for example, an aqueous potassium hydroxide (KOH) solution, an aqueous sodium hydroxide (NaOH) solution, or an aqueous lithium hydroxide (LiOH) solution. The electrolyte 8 may be a mixture of multiple alkaline aqueous solutions. In this embodiment, the electrolyte 8 is an alkaline mixed aqueous solution containing potassium hydroxide as the main component, sodium hydroxide, and lithium hydroxide. The electrolyte 8 may further contain other inorganic additives and organic additives.

2 is an enlarged view of region R2 in FIG. 1. The negative electrode collector 20 includes a base layer 210, a barrier layer 230, an alloy layer 250, and a plating layer 270. The negative electrode collector 20 is a laminate in which these layers 210, 230, 250, and 270 are stacked. In the negative electrode collector 20, the base layer 210, the barrier layer 230, the alloy layer 250, and the plating layer 270 are stacked in this order from the inside of the negative electrode collector 20 toward the collector outer surface 20a, which is the outer surface of the negative electrode collector 20. The base layer 210 is located at the center as the inside of the negative electrode collector 20, which is a laminate. The barrier layer 230 is stacked on the base layer 210. The alloy layer 250 is stacked on the barrier layer 230. The plating layer 270 is laminated on the alloy layer 250 and forms the current collector outer surface 20a. That is, as shown in FIG. 1, the plating layer 270 is provided at a position where it contacts at least one of the electrolyte solution 8 and the negative electrode active material 28.

In the negative electrode 2, when an aqueous electrolyte solution is used as the electrolyte solution 8, a charge/discharge reaction shown in the following formula (1) occurs. Specifically, zinc (Zn) as the negative electrode active material 28 reacts with hydroxy ions (OH ⁻ ) present in an ionized state in the electrolyte solution 8 and is oxidized. As a result, zinc hydroxide (Zn(OH) ₂ ) is produced and electrons (e ⁻ ) are generated. In the following formula (1), the reaction from the left side to the right side is the discharge reaction. Also, in the following formula (1), the reaction from the right side to the left side is the charge reaction.
Zn+2OH ⁻ →Zn(OH) ₂ +2e ⁻ Formula (1)

The underlayer 210 has a function as a collector that collects electrons generated by the reaction of the above formula (1) and a function as a support that supports the other layers 230, 250, and 270. The underlayer 210 is a conductor that is mainly composed of a metal having electrical conductivity. In this embodiment, the underlayer 210 is mainly composed of copper (Cu). The thickness of the underlayer 210 may be any thickness within a range in which the underlayer 210 can function as a collector and a support. The main component of the underlayer 210 is not limited to this. The underlayer 210 may be, for example, an alloy of copper and tin. The shape of the underlayer 210 may be, for example, a plate, foil, mesh, sponge, or fiber.

Here, in the case where an aqueous electrolyte is used as the electrolyte 8 in the negative electrode 2, hydrogen (H ₂ ) may be generated in the negative electrode 2 as shown in the following formula (2). Specifically, hydrogen is generated by contributing to a reaction that reduces water molecules (H ₂ O) in the electrolyte 8 without flowing to the positive electrode 5 side in the electrons generated in the above formula (1). When hydrogen is generated in the negative electrode 2, the generated hydrogen may adhere to the outer surface 2a of the negative electrode 2, thereby deteriorating the function of the battery 1. Therefore, in this embodiment, in the negative electrode current collector 20 constituting the negative electrode 2, an alloy layer 250 is provided between the barrier layer 230 and the plating layer 270 in order to suppress the generation of hydrogen in the negative electrode 2. The alloy layer 250 is a layer obtained by alloying the barrier layer 230 as the first base material and the plating layer 270 as the second base material. By providing the barrier layer 230, the alloy layer 250, and the plating layer 270, the generation of hydrogen in the negative electrode 2 can be suppressed. This will be described in detail later. Incidentally, hydrogen may also be generated at the negative electrode 2 when a non-aqueous electrolyte solution that has absorbed moisture is used.
2H ₂ O+2e ^- →H ₂ +2OH ^- Formula (2)

The barrier layer 230 covers the underlayer 210, thereby suppressing the diffusion of the conductive metal (copper in this embodiment) contained in the underlayer 210 toward the collector outer surface 20a. The barrier layer 230 also serves as a first base material for forming the alloy layer 250. The barrier layer 230 covers the entire surface of the underlayer 210 without any missing parts. The barrier layer 230 is formed on the underlayer 210 by, for example, electroplating. The barrier layer 230 may also be formed on the underlayer 210 by other methods such as hot-dip plating, vapor plating, or chemical plating.

The barrier layer 230 preferably has a thickness that does not allow the copper contained in the underlayer 210 to diffuse toward the collector outer surface 20a where the electrolyte 8 is present. Specifically, the thickness of the barrier layer 230 is preferably 2 μm or more and 10 μm or less. By making the thickness of the barrier layer 230 2 μm or more, the underlayer 210 can be covered by the barrier layer 230 without any loss. In addition, the upper limit of the thickness of the barrier layer 230 is set to 10 μm in consideration of the operability and cost when performing electroplating to cover the underlayer 210 with the barrier layer 230. Note that the thickness of the barrier layer 230 is not limited to this. The thickness of the barrier layer 230 may be, for example, more than 10 μm.

The barrier layer 230 is mainly composed of a transition metal. In this embodiment, the transition metal is, for example, at least one of nickel (Ni), iron (Fe), chromium (Cr), zirconium (Zr), and lanthanum (La). The transition metal as the main component of the barrier layer 230 preferably satisfies the following condition (i) in order to realize the protection of the underlayer 210 mainly composed of copper. In addition, the transition metal as the main component of the barrier layer 230 preferably satisfies the following condition (ii) in order to suppress the generation of hydrogen generated by the reaction formula (2) above. In order to suppress the generation of hydrogen in the negative electrode 2, a method of making the reaction that generates hydrogen as shown in the above formula (2) (hereinafter, hydrogen generation reaction) less likely to occur is considered. The following condition (ii) is an example of a condition for realizing the method of making the hydrogen generation reaction shown in the above formula (2) less likely to occur.
(i) A transition metal that can suppress the diffusion of copper from the underlayer 210 to the plating layer 270 forming the current collector outer surface 20a when the underlayer 210 containing copper as a main component is covered with the barrier layer 230. (ii) A transition metal that has a smaller exchange current density than gold (Au) in the hydrogen evolution reaction shown in the above formula (2).

As shown in the above condition (i), in order to suppress the diffusion of copper, which is the main component of the underlayer 210, toward the plating layer 270 forming the collector outer surface 20a, it is preferable to select a transition metal suitable for the barrier layer 230 covering the underlayer 210. In order to suppress the diffusion of copper contained in the underlayer 210 toward the plating layer 270, the transition metal preferably used for the plating layer 270 is, for example, nickel (Ni) or iron (Fe). In addition, in order to suppress the diffusion of copper contained in the underlayer 210 toward the plating layer 270, the transition metal not suitable for use in the plating layer 270 is, for example, indium (In), tin (Sn), or bismuth (Bi).

As shown in the above condition (ii), it is preferable to select a transition metal in which the hydrogen generation reaction shown in the above formula (2) is unlikely to occur as the main component of the barrier layer 230. In this embodiment, transition metals are divided into three groups according to the magnitude of the exchange current density related to the hydrogen generation reaction shown in the above formula (2). Specifically, the first group is a group in which the exchange current density related to the hydrogen generation reaction shown in the above formula (2) is greater than that of gold, and the second and third groups are groups in which the exchange current density related to the hydrogen generation reaction shown in the above formula (2) is smaller than that of gold. The second group is a transition metal whose exchange current density related to the hydrogen generation reaction shown in the above formula (2) is smaller than that of gold, but whose exchange current density related to the hydrogen generation reaction shown in the above formula (2) is greater than that of metals belonging to the third group. Note that some of the elements belonging to the third group do not fall under the category of transition metals, but will be described here in advance because they will be necessary in the plating layer 270 when described later.

The transition metals belonging to the first group are, for example, rhodium (Rh), rhenium (Re), iridium (Ir), or platinum (Pt). The transition metals belonging to the second group are, for example, nickel (Ni), iron (Fe), or cobalt (Co). The metals belonging to the third group are, for example, indium (In), tin (Sn), bismuth (Bi), or titanium (Ti). The transition metals belonging to the first group have a higher exchange current density for the hydrogen generation reaction shown in the above formula (2) than gold and relatively higher than the transition metals belonging to the second and third groups, so that the reaction shown in the above formula (2) may occur easily. On the other hand, the transition metals belonging to the second and third groups have a relatively lower exchange current density for the hydrogen generation reaction shown in the above formula (2) than the metals belonging to the first group, so that the reaction shown in the above formula (2) is less likely to occur than when the transition metals of the first group are used. Therefore, when the transition metals belonging to the second and third groups are used as the main components of the barrier layer 230, the possibility of the hydrogen generation reaction shown in the above formula (2) occurring can be reduced. Therefore, as shown in the above condition (ii), it is preferable to select, as the main component of the barrier layer 230, a transition metal belonging to the second and third groups whose exchange current density related to the hydrogen generation reaction shown in the above formula (2) is smaller than that of gold.

For the above reasons, in this embodiment, nickel is used as a transition metal that satisfies the above conditions (i) and (ii).

The barrier layer 230 may contain at least one of boron, aluminum, phosphorus, titanium, and cobalt, which is a different element from the transition metal that is the main component of the barrier layer 230. By containing a different element such as phosphorus in the barrier layer 230, an additional function such as reducing the solubility of the negative electrode active material 28 in the electrolyte 8 can be imparted.

The plating layer 270 is formed on the collector outer surface 20a to protect the inner layer, for example, the alloy layer 250. The plating layer 270 further serves as a second base material for forming the alloy layer 250. The plating layer 270 covers the entire surface of the barrier layer 230 without any missing parts. The surface of the barrier layer 230 here refers to the surface of the barrier layer 230 opposite to the surface in contact with the base layer 210. The plating layer 270 is formed on the barrier layer 230 by, for example, electroplating. The plating layer 270 may also be formed on the barrier layer 230 by other methods, such as hot-dip plating, vapor plating, or chemical plating.

The plating layer 270 is preferably thick enough to protect the alloy layer 250 and to obtain the desired thickness of the alloy layer 250 when the plating layer 270 and the barrier layer 230 are alloyed. Specifically, the thickness of the plating layer 270 is preferably 2 μm or more and 5 μm or less. If the plating layer 270 is thin, for example, less than 2 μm, pinholes may occur when covering the surface of the barrier layer 230, or the plating layer 270 formed on the barrier layer 230 may become uneven on the surface of the barrier layer 230. As a result, the barrier layer 230 may be exposed so as to come into contact with the electrolyte 8. In addition, the upper limit of the thickness of the plating layer 270 is set to 5 μm in consideration of operability and cost when performing electroplating to cover the barrier layer 230 with the plating layer 270. Note that the thickness of the plating layer 270 is not limited to this. The thickness of the plating layer 270 may be, for example, more than 10 μm.

The plating layer 270 is mainly composed of tin (Sn). There are four reasons for selecting tin as the main component of the plating layer 270. First, the inventors of the present application found that hydrogen generation in the negative electrode 2 can be suppressed by providing the alloy layer 250, which is an alloy of nickel and tin, on the negative electrode current collector 20. Second, as described above, tin has a small exchange current density related to the hydrogen generation reaction shown in the above formula (2), and is less likely to generate hydrogen. Third, tin is widely used as a plating material, and is excellent in the flexibility of the coating formed on the target object (in this embodiment, the barrier layer 230 and the alloy layer 250) and in the operability in plating work. Fourth, the corrosion resistance of the target object can be improved by covering the target object with tin. For the above reasons, in this embodiment, tin is used as the main component of the plating layer 270.

The plating layer 270 may contain at least one of indium (In) and bismuth (Bi) as an additive. Indium and bismuth are transition metals belonging to the third group, which have a smaller exchange current density for the hydrogen generation reaction shown in the above formula (2) than gold. Therefore, the exchange current density of the plating layer 270 can be made smaller than when the plating layer 270 does not contain at least one of indium and bismuth. Indium and bismuth can generally contribute to improving the corrosion resistance of the negative electrode active material 28.

The alloy layer 250 contributes to suppressing hydrogen generation in the negative electrode 2. Specifically, the negative electrode collector 20 retains hydrogen generated on the outer surface 2a of the negative electrode 2 in layers such as the alloy layer 250 located inside the collector outer surface 20a. The alloy layer 250 is formed by maintaining the laminated state in which the underlayer 210, the barrier layer 230, and the plating layer 270 are laminated in this order from the inside toward the collector outer surface 20a for a predetermined time. Specifically, when the laminated state is maintained, nickel, which is the main component of the barrier layer 230, and tin, which is the main component of the plating layer 270, are alloyed by natural diffusion. As a result, the alloy layer 250 is formed between the barrier layer 230 and the plating layer 270. In this embodiment, the alloy layer 250 is an alloy of nickel and tin.

When forming the alloy layer 250, the plating layer 270 may be heat-treated in a laminated state. For example, the plating layer 270 may be heated at 220°C for 10 minutes as the heat treatment. The heat treatment for the plating layer 270 is a so-called reflow treatment. By performing the heat treatment for the plating layer 270, the plating layer 270 can be made uniform. This can prevent the plating layer 270 from becoming non-uniform or having pinholes. Therefore, the possibility that the alloy layer 250 formed between the barrier layer 230 and the plating layer 270 is exposed to the collector outer surface 20a of the negative electrode collector 20 can be reduced. Note that the conditions such as the heating time and heating temperature in the heat treatment performed on the plating layer 270 are not limited to the above. The heating temperature in the heat treatment may be lower than 220°C. The heating time in the heat treatment may be longer or shorter than 10 minutes.

According to the above embodiment, the negative electrode current collector 20 includes a base layer 210, a barrier layer 230 mainly composed of a transition metal, an alloy layer 250 in which the transition metal of the barrier layer 230 and the tin of the plating layer 270 are alloyed, and a plating layer 270 mainly composed of tin. The base layer 210, the barrier layer 230, the alloy layer 250, and the plating layer 270 are stacked in this order from the inside toward the collector outer surface 20a. At this time, by including at least the barrier layer 230, the alloy layer 250, and the plating layer 270 in the negative electrode current collector 20, it is possible to suppress the generation of hydrogen in the negative electrode 2. In addition, when hydrogen is generated in the negative electrode 2, the hydrogen can be held in layers such as the alloy layer 250 located on the inside of the collector outer surface 20a. Therefore, it is possible to suppress the attachment of hydrogen to the outer surface 2a of the negative electrode 2. Therefore, it is possible to suppress the deterioration of the function of the battery 1 due to the attachment of hydrogen to the outer surface 2a of the negative electrode 2.

According to the above embodiment, an alkaline aqueous electrolyte is used as the electrolyte 8. In this case, the electrolyte 8 of this embodiment contains more hydroxy ions than an acidic or neutral electrolyte. The electrons generated by the reaction between the hydroxy ions and the negative electrode active material 28 shown in the above formula (1) flow to the positive electrode side, and the battery 1 realizes a discharge function. On the other hand, the electrons generated by the reaction between the hydroxy ions and the negative electrode active material 28 do not flow to the positive electrode side, but contribute to the reduction reaction of water in the electrolyte shown in the above formula (2), and the reaction shown in the above formula (2) occurs, and hydrogen may be generated in the negative electrode 2. Even in this case, the negative electrode current collector 20 includes at least the barrier layer 230, the alloy layer 250, and the plating layer 270, so that hydrogen can be retained in layers such as the alloy layer 250 located inside the collector outer surface 20a. Therefore, hydrogen generation in the negative electrode 2 can be suppressed. Therefore, the deterioration of the function of the battery 1 due to hydrogen attachment to the outer surface 2a of the negative electrode 2 can be suppressed.

According to the above embodiment, the barrier layer 230 is mainly composed of at least one transition metal selected from nickel, iron, chromium, zirconium, and lanthanum. In this case, the water in the electrolyte 8 is oxidized as shown in the above formula (2) due to electrons generated by the reaction shown in the above formula (1), and hydrogen is generated. When hydrogen is generated at the negative electrode 2, the barrier layer 230 can be formed by a transition metal whose exchange current density related to the hydrogen generation reaction is smaller than that of gold. Therefore, the hydrogen generation reaction shown in the above formula (2) is less likely to occur compared to when the barrier layer 230 is formed by a transition metal whose exchange current density related to the hydrogen generation reaction is larger than that of gold. Therefore, the barrier layer 230 can be formed by a transition metal that can suppress the generation of hydrogen at the negative electrode 2.

In addition, in the above embodiment, the thickness of the barrier layer 230 is set to 2 μm or more and 10 μm or less. In this way, the base layer 210 can be covered by the barrier layer 230 without any gaps. This reduces the possibility that the base layer 210 is exposed on the barrier layer 230. This reduces the possibility that the metal contained in the base layer 210 diffuses toward the current collector outer surface 20a.

In addition, in the above embodiment, the thickness of the plating layer 270 is set to 2 μm or more and 5 μm or less. In this way, the alloy layer 250 can be covered without any loss by the plating layer 270. Therefore, when hydrogen is generated in the negative electrode 2, the possibility that layers such as the alloy layer 250, which have the function of retaining hydrogen, are exposed to the current collector outer surface 20a can be reduced. Therefore, the generation of hydrogen in the negative electrode 2 can be more reliably suppressed.

In addition, according to the above embodiment, the barrier layer 230 may contain at least one of boron, aluminum, phosphorus, titanium, and cobalt, which is a different element from the transition metal that is the main component of the barrier layer 230. By containing a different element such as phosphorus in the barrier layer 230, an additional function such as reducing the solubility of the negative electrode active material 28 in the electrolyte 8 can be imparted.

In addition, according to the above embodiment, the plating layer 270 can be configured to contain at least one of the elements indium and bismuth. That is, the plating layer 270 contains a metal whose exchange current density in the hydrogen generation reaction shown in the above formula (2) is smaller than that of gold and is equal to or smaller than that of tin. This makes it possible to reduce the exchange current density of the plating layer 270 in the hydrogen generation reaction shown in the above formula (2). Therefore, hydrogen generation in the negative electrode 2 can be further suppressed.

In addition, according to the above embodiment, the plating layer 270 is heat-treated in a laminated state in which the base layer 210, the barrier layer 230, and the plating layer 270 are laminated in this order from the inside toward the current collector outer surface 20a. This makes it possible to homogenize the plating layer 270. In other words, it is possible to reduce the possibility that the plating layer 270 will become non-uniform or that pinholes will occur. Therefore, in a state in which the alloy layer 250 is formed between the barrier layer 230 and the plating layer 270, it is possible to reduce the possibility that the alloy layer 250 will be exposed to the current collector outer surface 20a.

A-2. Experimental example:
A-2-1. Experimental Example 1:
On the premise of the configuration described above, samples X1 to X4 as the negative electrode 2 of this embodiment and sample Y1 as a comparative example were produced. In this experiment, the sample Y1 as a comparative example was compared with the samples X1 to X4 of this embodiment to confirm the difference in hydrogen generation in the negative electrode 2 depending on the presence or absence of the barrier layer 230, the alloy layer 250, and the plating layer 270. The sample Y1 as a comparative example differs from the samples X1 to X4 in the configuration of the negative electrode current collector 20. Specifically, the negative electrode current collector 20 of sample Y1 does not include the barrier layer 230 and the plating layer 270. As a result, the negative electrode current collector 20 of sample Y1 does not include the barrier layer 230, the alloy layer 250, and the plating layer 270.

Sample X1 was prepared as follows. From the viewpoint of electrical conductivity and workability, the underlayer 210 was a punched metal made of oxygen-free copper (C1020). The barrier layer 230 was formed on the underlayer 210 without any defects. The thickness of the barrier layer 230 was set to 2 μm. Next, the plating layer 270 was formed on the barrier layer 230 without any defects. The thickness of the plating layer 270 was set to 3 μm. Next, the underlayer 210, the barrier layer 230, and the plating layer 270 were stacked in this order from the inside toward the collector outer surface 20a, and the stacked state was maintained for a predetermined time. As a result, an alloy layer 250 was formed between the barrier layer 230 and the plating layer 270. The stacked body in which these layers 210, 230, 250, and 270 were stacked was used as the negative electrode collector 20.

In producing the negative electrode active material 28, powdered zinc oxide, powdered zinc, carboxymethyl cellulose, and a dispersion liquid in which polytetrafluoroethylene was dispersed were mixed in a weight ratio of 90:10:1:2 to obtain a first mixed liquid. A suitable amount of a solution in which water and isopropanol (IPA) were mixed in a weight ratio of 1:1 was dropped into the first mixed liquid to obtain a second mixed liquid. The second mixed liquid was stirred for 15 minutes using a Thinky Planetary Rotation and Revolution Mixer to obtain a slurry-like ink, which was used as the negative electrode active material 28.

In producing the negative electrode 2, the negative electrode active material 28 was applied to the negative electrode current collector 20 so that about 100 mg of the negative electrode active material 28 was applied to ^{1 cm2} of the negative electrode current collector 20, thereby obtaining a negative electrode mixture. The negative electrode mixture was dried at 80°C for 2 hours, and then pressed at a linear pressure of 0.75t using a roll press machine manufactured by Takumi Giken Co., Ltd. to obtain the negative electrode 2.

The first separator C1 was formed from a polypropylene porous film and a mixed nonwoven fabric made of a mixture of polyvinyl alcohol fibers and cellulose fibers. After a copper foil with a thickness of 120 μm was welded to one end of the negative electrode 2 using a resistance welding machine, the negative electrode 2 was wrapped in the first separator C1 to form a negative electrode-separator composite.

The positive electrode current collector 50 was made of "Celmet (registered trademark)" manufactured by Sumitomo Electric Industries, Ltd., a porous metal whose main component is nickel. A positive electrode terminal was welded to the positive electrode 5, which was composed of the positive electrode current collector 50 and nickel hydroxide as the positive electrode active material 58, and then stacked to obtain a positive electrode composite. The second separator C2 was made of nonwoven fabric. The positive electrode composite was welded and embedded in the second separator C2 to form a positive electrode-separator composite.

The negative electrode-separator composite and the positive electrode-separator composite were placed in the space formed by the battery container body and the bottom lid, and a predetermined amount of electrolyte 8 was added. The electrolyte 8 was an alkaline mixed aqueous solution containing potassium hydroxide as the main component, sodium hydroxide aqueous solution, and lithium hydroxide aqueous solution. This resulted in the negative electrode-separator composite and the positive electrode-separator composite being immersed in the electrolyte 8. The top lid was then sealed to obtain sample X1.

Sample X2 is a sample in which heat treatment was performed on the plating layer 270 of the negative electrode current collector 20 of Sample X1. In Sample X2, the plating layer 270 was subjected to heat treatment in a laminated state in which the base layer 210, the barrier layer 230, and the plating layer 270 were laminated in this order from the inside toward the collector outer surface 20a. Specifically, in the laminated state, the plating layer 270 was heated at 220°C for 10 minutes to melt the plating layer 270. The heated plating layer 270 was then quenched to obtain Sample X2. The other components of Sample X2 and the method of producing Sample X2 were the same as those of Sample X1.

Sample X3 is a sample in which the barrier layer 230 in the negative electrode current collector 20 of sample X1 contains phosphorus as a different element different from the main component of the barrier layer 230. The other components of sample X3 and the method for producing sample X3 are the same as those of sample X1.

Sample X4 is a sample in which the thickness of the barrier layer 230 and the plating layer 270 in the negative electrode current collector 20 of sample X1 are each made thinner. In sample X4, the thickness of the barrier layer 230 is 1 μm, and the thickness of the plating layer 270 is 2 μm. The other components of sample X4 and the method of producing sample X4 are the same as those of sample X1.

Sample Y1, which is a comparative example, is a sample that does not have the barrier layer 230, the alloy layer 250, and the plating layer 270 that are provided on the negative electrode current collector 20 of sample X1. The other components of sample Y1 and the method for producing sample Y1 are the same as those of sample X1.

Figure 3 shows the measurement results by cyclic voltammetry using the fabricated negative electrode 2. Figure 3 shows the measurement results of samples X1 to X4 and sample Y1 as a comparative example.

Cyclic voltammetry is a basic measurement technique in the field of electrochemistry, in which the electrode potential is repeatedly swept and the response current during the sweep is measured. In the measurement shown in FIG. 3, one of samples X1 to X4, and Y1, a nickel counter electrode, and a mercury-mercury oxide electrode as a reference electrode were placed in an electrochemical cell. A 6 mol/L aqueous potassium hydroxide solution was added to this electrochemical cell as electrolyte 8. In this state, a round trip sweep was performed between -1.2 V and -1.9 V relative to the reference electrode potential (SHE ratio +0.10 V). In other words, in the measurement shown in FIG. 3, a negative sweep from -1.2 V to -1.9 V and a positive sweep from -1.9 V to -1.2 V were performed once each relative to the reference electrode potential (SHE ratio +0.10 V).

The horizontal axis of Fig. 3 represents the potential of the reference electrode. In Fig. 3, the unit of the potential of the reference electrode is [V]. The vertical axis of Fig. 3 represents the response current value versus potential. In Fig. 3, the unit of the response current value is [mA]. The graph in Fig. 3 is a so-called cyclic voltammogram, which shows the progression of changes in the response current value at a specific potential. In Fig. 3, the average value of the positive sweep and the negative sweep between -1.2 V and -1.9 V is shown as a single graph. In the cyclic voltammogram, a peak representing the potential difference occurs near the redox potential. In Fig. 3, the peak formed in the direction in which the response current value becomes negative is a reduction wave generated by fluctuations in the reduction side current. The peak formed in the direction in which the response current value becomes positive is an oxidation wave generated by fluctuations in the oxidation side current.

3, in sample Y1, in which the barrier layer 230, the alloy layer 250, and the plating layer 270 are not provided on the negative electrode current collector 20, the reduction-side current is greatly reduced when the potential of the reference electrode is near -1.9 V. In contrast, in sample X1, in which the barrier layer 230, the alloy layer 250, and the plating layer 270 are provided on the negative electrode current collector 20, the reduction-side current is near -3.0 mA when the potential of the reference electrode is -1.9 V. In other words, when the potential of the reference electrode is -1.9 V, sample X1 has a smaller reduction-side current than sample Y1. In other words, when the potential of the reference electrode is -1.9 V, sample X1 has a smaller reduction wave than sample Y1. In this embodiment, the point when the potential of the reference electrode is near -1.9 V corresponds to the oxidation-reduction potential of the hydrogen generation reaction shown in the above formula (2).

Here, the magnitude of the reduction wave is proportional to the amount of electrons supplied to the negative electrode 2. That is, when the reduction wave is large, more electrons are supplied to the negative electrode 2, and the reduction reaction proceeds actively. On the other hand, the smaller the reduction wave, the fewer electrons are supplied to the negative electrode 2, and the reduction reaction is suppressed. Therefore, compared to sample Y1, sample X1 is able to suppress the generation of hydrogen in the negative electrode 2 including the negative electrode current collector 20. That is, when the barrier layer 230, the alloy layer 250, and the plating layer 270 are provided in the negative electrode current collector 20 constituting the negative electrode 2, the generation of hydrogen in the negative electrode 2 can be suppressed.

Furthermore, in Figure 3, in sample X1, when the potential of the reference electrode is in the range of -1.5 to -1.4 V, a fluctuation is observed in the oxidation side current, and an oxidation wave is formed. In contrast, in sample Y1, when the potential of the reference electrode is in the range of -1.5 to -1.4 V, no fluctuation is observed in the oxidation side current, and no oxidation wave is formed.

The size of the oxidation wave is proportional to the amount of electrons lost from the negative electrode 2 side. Specifically, when the oxidation wave is formed, an oxidation reaction occurs on the negative electrode 2 side as a reaction in which electrons are lost. Therefore, even if hydrogen is generated on the negative electrode 2, it is considered that the sample X1 can suppress the adhesion of hydrogen to the outer surface 2a of the negative electrode 2 due to the oxidation reaction that occurs when the potential of the reference electrode becomes approximately -1.5 to -1.4 V. The oxidation reaction that occurs when the potential of the reference electrode becomes approximately -1.5 to -1.4 V is, for example, a reaction in which hydrogen is oxidized to generate water, as shown in the following formula (3). It can also be said that a layer such as the alloy layer 250 located inside the current collector outer surface 20a has an oxidation-reduction ability.
2H ₂ +O ₂ →2H ₂ O Formula (3)

The larger the oxidation wave is at the point when the potential of the reference electrode is in the range of -1.5 to -1.4 V, the more actively the oxidation reaction shown in the above formula (3) is progressing. In other words, the larger the oxidation wave is, the greater the proportion of hydrogen generated by the reaction formula (2) above that is oxidized to produce water, and therefore the amount of hydrogen adhering to the outer surface 2a of the negative electrode 2 is thought to decrease.

In addition, by providing the barrier layer 230, the alloy layer 250, and the plating layer 270 in the negative electrode current collector 20, it is thought that layers such as the alloy layer 250 located inside the collector outer surface 20a function like a hydrogen storage alloy. Specifically, the negative electrode current collector 20 absorbs hydrogen generated in the negative electrode 2 to form a metal hydride. In other words, layers such as the alloy layer 250 located inside the collector outer surface 20a hold hydrogen. In this way, it is possible that hydrogen generation in the negative electrode 2 is suppressed by storing hydrogen in the form of a metal hydride in the negative electrode current collector 20.

The larger the oxidation wave is at the time when the potential of the reference electrode is in the range of -1.5 to -1.4 V, the more actively the formation of metal hydrides is thought to proceed. In other words, the larger the oxidation wave, the greater the amount of hydrogen absorbed in layers such as the alloy layer 250 located inside the current collector outer surface 20a, and the less hydrogen adheres to the outer surface 2a of the negative electrode 2. It is also possible that hydrogen held in layers such as the alloy layer 250 located inside the current collector outer surface 20a is oxidized by the reaction formula (3) above.

In addition, in the heat-treated sample X2, the reduction-side current at the time when the potential of the reference electrode becomes -1.9 V is approximately -2.5 mA. That is, at the time when the potential of the reference electrode becomes -1.9 V, the reduction-side current of sample X2 is smaller than that of sample Y1 as a comparative example, similar to sample X1. At the time when the potential of the reference electrode becomes -1.9 V, the reduction-side current of sample X2 is smaller than that of sample X1. As shown in FIG. 3, in sample X2, at the time when the potential of the reference electrode becomes approximately -1.5 to -1.4 V, the oxidation-side current fluctuates and an oxidation wave is formed, similar to sample X1. At this time, the oxidation wave of sample X2 has a larger peak than the oxidation wave of sample X1. From this, by performing a heat treatment on the plating layer 270 in the process of forming the alloy layer 250, the generation of hydrogen in the negative electrode 2 can be further suppressed.

In sample X3, in which phosphorus is added to the barrier layer 230, the reduction side current at the time when the potential of the reference electrode becomes -1.9 V is approximately -2.4 mA. That is, at the time when the potential of the reference electrode becomes -1.9 V, sample X3, like sample X1, has a smaller reduction side current than sample Y1 as a comparative example. Also, at the time when the potential of the reference electrode becomes -1.9 V, the reduction side current of sample X3 is smaller than the reduction side currents of samples X1 and X2. As shown in FIG. 3, in sample X3, like sample X1, a fluctuation in the oxidation side current is observed at the time when the potential of the reference electrode becomes approximately -1.5 to -1.4 V, and an oxidation wave is formed. From this, by including phosphorus as a different element different from the main component of the barrier layer 230 in the barrier layer 230, the generation of hydrogen in the negative electrode 2 can be further suppressed.

In sample X4, in which the thickness of the barrier layer 230 and the thickness of the plating layer 270 are thinner than those of sample X1, the reduction side current at the time when the potential of the reference electrode is near -1.9 V is near -4.5 mA. In other words, at the time when the potential of the reference electrode is near -1.9 V, the reduction side current of sample X4 is smaller than that of sample Y1 as a comparative example, but is larger than that of samples X1 to X3. In addition, at the time when the potential of the reference electrode is near -1.9 V, the reduction side current value of sample X4 shows a value closer to that of sample Y1 than that of samples X1 to X3. From this, even when the thickness of the barrier layer 230 is 1 μm and the thickness of the plating layer 270 is 2 μm, the generation of hydrogen in the negative electrode 2 can be suppressed by providing the barrier layer 230, the alloy layer 250, and the plating layer 270 in the negative electrode current collector 20. On the other hand, compared to when the barrier layer 230 is 2 μm thick and the plating layer 270 is 3 μm thick, when the barrier layer 230 is 1 μm thick and the plating layer 270 is 2 μm thick, it is difficult to obtain the effect of suppressing hydrogen generation in the negative electrode 2. Therefore, it is more preferable that the barrier layer 230 is 2 μm thick or more and the plating layer 270 is 3 μm thick or more.

A-2-2. Experimental Example 2:
Furthermore, in order to compare the performance of the battery 1, a cycle endurance test was conducted on the samples X1 to X4 and the sample Y1. FIG. 4 is a diagram showing the conditions of the cycle endurance test. In this test, the samples X1 to X4 as the battery 1 of the present embodiment and the sample Y1 as the comparative example were repeatedly charged and discharged, and the performance of the samples X1 to X4 and Y1 was evaluated by measuring the number of charge/discharge cycles until the functions of the samples X1 to X4 and Y1 deteriorated. In the initial state before the start of this test, the samples X1 to X4 and Y1 had a full charge capacity of 120 mAh and a remaining capacity (SOC) of 100%.

As shown in FIG. 4, in this test, the charging process and the discharging process were repeatedly performed. Between each of the charging and discharging processes, a waiting time of 5 minutes was provided during which neither the charging process nor the discharging process was performed. In this test, one cycle consisted of a charging process, a first waiting time after the charging process and before the discharging process, and a discharging process, and a second waiting time after the discharging process and before the charging process as the time when the next cycle was started. The charging process was performed by the CC-CV method, which combines constant current charging and constant voltage charging. Specifically, in the charging process, a current of 1C was supplied to samples X1 and Y1 until the voltage reached 2.00V, and then a current of 60mA was supplied while maintaining the voltage at 2.00V. When a predetermined termination condition indicating the completion of charging was reached, the charging process in this cycle was terminated. The discharging process was performed by the constant current discharge (CC) method. Specifically, in the discharging process, a current of 1C was supplied to samples X1 and Y1 until the voltage reached 1.1V.

Figure 5 shows the results of the cycle durability test. Figure 5 shows the test results for samples X1 to X4 as the battery 1 of this embodiment and sample Y1 as a comparative example. In this test, the number of cycles until the battery capacity ratio of samples X1 to X4 and Y1 decreased to 30% was measured, assuming that the battery capacity at the start was 100%, and the time point at which the charge/discharge function of samples X1 to X4 and Y1 decreased was determined. As shown in Figure 5, sample Y1, which does not have a barrier layer 230, alloy layer 250, and plating layer 270 on the negative electrode current collector 20, reached a battery capacity ratio of 30% at 25 cycles. In contrast, sample X1, which has a barrier layer 230, alloy layer 250, and plating layer 270 on the negative electrode current collector 20, reached a battery capacity ratio of 30% at 154 cycles. That is, by providing the barrier layer 230, the alloy layer 250, and the plating layer 270 in the negative electrode current collector 20, the number of cycles until the battery capacity ratio decreases to 30% can be increased. Therefore, the deterioration of the function of the battery 1 can be suppressed.

The heat-treated sample X2 reached a battery capacity ratio of 30% after 160 cycles. This shows that by subjecting the plating layer 270 of the negative electrode current collector 20 to heat treatment, the number of cycles until the battery capacity ratio drops to 30% can be further increased.

Sample X3, in which phosphorus was added to the barrier layer 230, reached a battery capacity ratio of 30% at 255 cycles. This shows that by including a different element in the barrier layer 230, the number of cycles until the battery capacity ratio drops to 30% can be further increased.

In sample X4, in which the thickness of the barrier layer 230 and the thickness of the plating layer 270 are thinner than those of sample X1, the battery capacity ratio reaches 30% after 60 cycles. From this, even if the thickness of the barrier layer 230 is 1 μm and the thickness of the plating layer 270 is 2 μm, the number of cycles until the battery capacity ratio drops to 30% can be increased by providing the barrier layer 230, the alloy layer 250, and the plating layer 270. On the other hand, the increase in the number of cycles of sample X4 is smaller than that of sample Y1 compared to samples X1 to X3. That is, compared to when the thickness of the barrier layer 230 is 2 μm and the thickness of the plating layer 270 is 3 μm, it is difficult to increase the number of cycles compared to sample Y1 when the thickness of the barrier layer 230 is 1 μm and the thickness of the plating layer 270 is 2 μm. Therefore, it is more preferable to set the thickness of the barrier layer 230 to 2 μm or more and the thickness of the plating layer 270 to 3 μm or more.

B. Other embodiments:
In the above embodiment, the type of the battery 1 is a nickel-zinc secondary battery, but the present disclosure is not limited to this. The battery 1 may be, for example, a primary battery. Even in such a form, hydrogen is generated in the negative electrode 2 including the negative electrode current collector 20, and the hydrogen can be prevented from adhering to the outer surface 2 a of the negative electrode 2.

The present disclosure is not limited to the above-described embodiments, and can be realized in various configurations without departing from the spirit of the present disclosure. For example, the technical features of the embodiments corresponding to the technical features in each form described in the Summary of the Invention column can be replaced or combined as appropriate to solve some or all of the above-described problems or to achieve some or all of the above-described effects. Furthermore, if a technical feature is not described as essential in this specification, it can be deleted as appropriate.

1...battery, 2...negative electrode, 2a...outer surface, 5...positive electrode, 8...electrolyte, 20...negative electrode collector, 20a...collector outer surface, 28...negative electrode active material, 50...positive electrode collector, 58...positive electrode active material, 210...underlayer, 230...barrier layer, 250...alloy layer, 270...plating layer, C1...first separator, C2...second separator

Claims (7)

A negative electrode current collector for a battery using an electrolyte, comprising:
A base layer mainly composed of a conductive metal;
a barrier layer formed on the underlayer and containing a transition metal as a main component;
an alloy layer formed on the barrier layer and in which the transition metal and tin are alloyed;
a plating layer containing tin as a main component and laminated on the alloy layer,
the barrier layer contains at least one of boron, aluminum, phosphorus, titanium, and cobalt, which is a different element from the transition metal that is the main component of the barrier layer . The negative electrode current collector according to claim 1 ,
The electrolyte is an alkaline aqueous electrolyte. The negative electrode current collector according to claim 1 or 2,
The negative electrode current collector, wherein the transition metal is at least one of nickel, iron, chromium, zirconium, and lanthanum. The negative electrode current collector according to any one of claims 1 to 3,
The negative electrode current collector, wherein the barrier layer has a thickness of 2 μm or more and 10 μm or less. The negative electrode current collector according to any one of claims 1 to 4,
The negative electrode current collector, wherein the plating layer has a thickness of 2 μm or more and 5 μm or less. The negative electrode current collector according to any one of claims 1 to 5 ,
The negative electrode current collector, wherein the plating layer further contains at least one of indium and bismuth. A battery,
A negative electrode comprising the negative electrode current collector according to any one of claims 1 to 6 and a negative electrode active material;
a positive electrode including a positive electrode current collector and a positive electrode active material;
a separator separating the negative electrode and the positive electrode;
a battery comprising: an electrolyte contained in a region in which the negative electrode, the positive electrode, and the separator are disposed.

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