Hydrogen storage alloy negative electrode and nickel-hydrogen secondary battery including the hydrogen storage alloy negative electrode

Abstract

To provide a hydrogen storage alloy negative electrode that improves cycle life characteristics and low-temperature charge characteristics.SOLUTION: A hydrogen storage alloy negative electrode includes a hydrogen storage alloy and yttrium fluoride as an additive. The mass of yttrium fluoride is 0.1 mass part or more and 0.2 mass part or less per 100 mass parts of hydrogen storage alloy powder.SELECTED DRAWING: Figure 1

Description

[Technical Field]

[0001] The present invention relates to a hydrogen storage alloy negative electrode and a nickel-metal hydride secondary battery including the hydrogen storage alloy negative electrode. [Background technology]

[0002] Nickel-metal hydride secondary batteries have a higher capacity and are environmentally safer than nickel-cadmium secondary batteries, and are therefore used in a variety of devices, such as portable electronic devices, power tools, and hybrid electric vehicles, and their applications are expanding. As these applications expand, there is a demand for higher performance nickel-metal hydride secondary batteries, and improving their cycle life characteristics in particular has become an important issue (Patent Document 1). In other words, there is a demand for improving cycle life characteristics so that the number of times a battery can be charged and discharged can be increased, and a great deal of research is being conducted on this issue.

[0003] To extend the cycle life, for example, a technique of adding rare earth fluorides as additives to the negative electrode active material mixture has been proposed (Patent Document 2). These materials prevent the hydrogen-absorbing alloy containing hydrogen, which is the negative electrode active material, from being corroded by the highly concentrated alkali electrolyte, thereby improving the cycle life characteristics. [Prior art documents] [Patent documents]

[0004] [Patent Document 1] Japanese Patent Application Publication No. 8-329934 [Patent Document 2] Japanese Patent Application Laid-Open No. 2016-149299 Summary of the Invention [Problem to be solved by the invention]

[0005] However, when rare earth fluorides are added at a certain concentration or higher, there is a problem in that the dischargeable capacity decreases when charging in a low-temperature environment below freezing, such as -10°C. That is, the low-temperature charging characteristics are deteriorated. In this disclosure, the "low-temperature charging characteristics" refers to the maximum capacity that can be discharged in a room-temperature environment after charging at a temperature below room temperature, such as -10°C or below freezing, whereas normal charging characteristics indicate the maximum charge capacity when charging at room temperature (25°C).

[0006] Therefore, an object of the present invention is to provide a hydrogen storage alloy negative electrode that achieves both cycle life characteristics and low-temperature charging characteristics, and a nickel-metal hydride secondary battery including such a hydrogen storage alloy negative electrode. [Means for solving the problem]

[0007] In order to achieve the above object, the hydrogen storage alloy negative electrode of the present invention is characterized in that it contains a hydrogen storage alloy and yttrium fluoride as an additive, and the mass of the yttrium fluoride is 0.1 to 0.2 parts by mass per 100 parts by mass of the hydrogen storage alloy powder. [Effects of the Invention]

[0008] According to the hydrogen storage alloy negative electrode of the present invention, in a nickel-metal hydride secondary battery including such a hydrogen storage alloy negative electrode, it is possible to improve not only the charge / discharge cycle life but also the low-temperature charging characteristics. [Brief explanation of the drawings]

[0009] [Figure 1] 1 is a partially cutaway perspective view of a nickel-metal hydride secondary battery according to an embodiment of the present invention; [Figure 2] 1 is a table showing low-temperature charging characteristics and cycle life characteristics. [Figure 3] 1 is a graph showing changes in low-temperature charging characteristics and cycle life characteristics with respect to the amount of yttrium fluoride added. DETAILED DESCRIPTION OF THE INVENTION

[0010] 1. Structure and manufacturing of nickel-metal hydride secondary batteries A nickel-metal hydride secondary battery (hereinafter referred to as the battery) 2 according to the present disclosure will be described with reference to the drawings.

[0011] For example, while FIG. 1 shows an AA-sized cylindrical battery 2, the size of the battery 2 to which the present disclosure is applied is not limited to the AA size.

[0012] As shown in FIG. 1 , the battery 2 includes a cylindrical outer can 10 with a bottom and an open top. The bottom wall 35 of the outer can 10 is conductive and functions as a negative electrode terminal. A sealing body 11 is fixed to the opening of the outer can 10. This sealing body 11 includes a lid plate 14 and a positive electrode terminal 20, seals the outer can 10, and constitutes the positive electrode terminal 20. A conductive, disc-shaped lid plate 14 and a ring-shaped insulating gasket 12 surrounding the lid plate 14 are disposed within the opening of the outer can 10. The insulating gasket 12 is fixed to the opening edge 37 of the outer can 10 by crimping. That is, the lid plate 14 and the insulating gasket 12 cooperate to hermetically close the opening of the outer can 10.

[0013] The cover plate 14 has a gas vent hole 16 in the center, and a rubber valve element 18 that closes the gas vent hole 16 is disposed on the outer surface of the cover plate 14. Furthermore, a flanged, cylindrical positive electrode terminal 20 is fixed to the outer surface of the cover plate 14 so as to cover the valve element 18, and the positive electrode terminal 20 presses the valve element 18 toward the cover plate 14. The positive electrode terminal 20 is provided with a vent hole (not shown). Normally, the gas vent hole 16 is airtightly closed by the valve element 18. However, when gas is generated inside the outer can 10 and the internal pressure increases, the valve element 18 is compressed by the internal pressure, opening the gas vent hole 16. This allows gas to be released from inside the outer can 10 through the gas vent hole 16 and the vent hole in the positive electrode terminal 20. In other words, the gas vent hole 16, the valve element 18, and the positive electrode terminal 20 form a safety valve for the battery.

[0014] The outer can 10 accommodates an electrode group 22. The electrode group 22 is composed of a strip-shaped positive electrode 24, a strip-shaped negative electrode 26, and a strip-shaped separator 28, and is spirally wound with the separator 28 sandwiched between the positive electrode 24 and the negative electrode 26. That is, the positive electrode 24 and the negative electrode 26 face each other with the separator 28 interposed between them, and are overlapped in the radial direction of the outer can 10.

[0015] Within the exterior can 10, a positive electrode lead 30 is disposed between one end of the electrode group 22 and the cover plate 14, and each end of the positive electrode lead 30 is connected to the positive electrode 24 and the cover plate 14, respectively. That is, the positive electrode terminal 20 of the cover plate 14 and the positive electrode 24 are electrically connected to each other via the positive electrode lead 30 and the cover plate 14. A circular insulating member 32 is disposed between the cover plate 14 and the electrode group 22, and the positive electrode lead 30 extends through a slit 39 provided in the insulating member 32. A circular insulating member 34 is also disposed between the electrode group 22 and the bottom of the exterior can 10.

[0016] A predetermined amount of alkaline electrolyte (not shown) is poured into the exterior can 10. The alkaline electrolyte impregnates the positive electrode 24, the negative electrode 26, and the separator 28 and participates in the charge / discharge reaction between the positive electrode 24 and the negative electrode 26. While not particularly limited, this alkaline electrolyte is preferably an alkaline electrolyte containing NaOH as a solute. In this embodiment, the alkaline electrolyte preferably contains, as a solute, at least one of KOH and LiOH in addition to NaOH. For example, an electrolyte containing NaOH solution and LiOH solution in a ratio of 8.0:0.7 is used. Using an electrolyte with a high sodium content is desirable, as this increases the overvoltage required for the water splitting reaction and further improves charging efficiency.

[0017] In the electrode group 22, the separator 28 is not wound around the outer periphery, and the outermost periphery of the negative electrode 26 forms the outer periphery of the electrode group 22. This outer surface comes into contact with the peripheral wall of the outer can, thereby electrically connecting the negative electrode 26 and the outer can 10 to each other.

[0018] Separator 28 is preferably made of, for example, a nonwoven fabric made of sulfonated polypropylene fibers. The sulfonic acid groups capture metal ions dissolved in the electrolyte and prevent the metal ions from depositing on the surfaces of the positive and negative electrode active materials. Sulfonation of separator 28 not only imparts hydrophilicity to the separator but also prevents the deposition of dissolved metal ions on the active material surfaces, which can degrade the charging temperature characteristics and cycle life characteristics. This also contributes to suppressing self-discharge of battery 2.

[0019] The positive electrode 24 comprises a conductive positive substrate having a porous structure and a positive electrode mixture held in the pores of the positive substrate and on the surface of the positive substrate. The positive substrate may be, for example, a nickel-plated mesh-like, sponge-like, or fibrous metal body or nickel foam.

[0020] The positive electrode mixture contains positive electrode active material particles, a conductive material, a positive electrode additive, and a binder. The positive electrode active material particles are nickel hydroxide particles or higher-order nickel hydroxide particles. It is preferable that at least one of zinc, magnesium, and cobalt is solid-dissolved in the nickel hydroxide particles.

[0021] The positive electrode additive is appropriately selected and added as needed to improve the characteristics of the positive electrode. Examples of the main positive electrode additives include yttrium oxide and zinc oxide.

[0022] The conductive material may be, for example, one or more selected from cobalt (Co) and cobalt compounds such as cobalt oxide (CoO) and cobalt hydroxide (Co(OH)2). This conductive material is added to the positive electrode mixture as needed, and may be added in the form of a powder or in the form of a coating that covers the surface of the positive electrode active material and is included in the positive electrode mixture.

[0023] The binder functions to bind the positive electrode active material particles, the conductive material, and the positive electrode additive, and also to bind the positive electrode mixture to the positive electrode substrate. Examples of the binder that can be used here include carboxymethyl cellulose, methyl cellulose, polytetrafluoroethylene (PTFE) dispersion, and hydroxypropyl cellulose (HPC) dispersion.

[0024] These positive electrode active material particles, a conductive material, a positive electrode additive, a binder, and water are mixed together to prepare a positive electrode active material slurry.

[0025] For example, while stirring a mixed aqueous solution of nickel sulfate, zinc sulfate, magnesium sulfate, and cobalt sulfate, an aqueous solution of sodium hydroxide is gradually added so that the ratio of zinc to metal nickel is 3% by weight, magnesium to 0.4% by weight, and cobalt to 1% by weight, and the pH during the reaction is stabilized at 13 to 14 to elute nickel hydroxide. This is then washed three times with 10 times the amount of pure water, and then subjected to dehydration and drying processes to produce a nickel hydroxide active material.

[0026] Next, this nickel hydroxide active material is mixed with 10 wt% cobalt hydroxide, 0.5 wt% yttrium oxide, 40 wt% hydroxypropyl cellulose (HPC) dispersion, and 0.3 wt% zinc oxide to prepare a positive electrode active material slurry. This positive electrode active material slurry is filled into a positive electrode substrate, dried, rolled, and cut to a predetermined size to prepare a nickel positive electrode plate.

[0027] The negative electrode 26 has a strip-shaped conductive negative electrode core, and a negative electrode mixture is supported on this negative electrode core. The negative electrode core is made of a sheet-like metal material with distributed through holes, such as a punched iron sheet with a nickel-plated surface. When held on the negative electrode core, the negative electrode mixture forms a negative electrode mixture layer.

[0028] The negative electrode mixture contains particles of a hydrogen storage alloy, a negative electrode additive, a conductive material, and a binder.

[0029] The hydrogen storage alloy is an alloy capable of absorbing and releasing hydrogen, which is a negative electrode active material. A typical hydrogen storage alloy can be used as the hydrogen storage alloy. In the present disclosure, it is preferable to use a rare earth-Mg-Ni-based hydrogen storage alloy containing rare earth elements, Mg, and Ni.

[0030] The hydrogen storage alloy particles can be obtained, for example, as follows.

[0031] La, Mg, Ni, and Al are weighed and mixed to achieve the desired composition. The mixture is melted in a high-frequency induction melting furnace in an argon gas atmosphere, poured into a mold, and cooled to room temperature to obtain an alloy ingot. This alloy ingot is then placed in a metal container, the interior of the container is flushed with argon gas, and sealed. The container is then placed in a heat treatment furnace and heat-treated at a temperature of 900°C to 1000°C for 10 hours. After cooling, the alloy ingot is crushed and sieved to obtain hydrogen-absorbing alloy particles of the desired particle size.

[0032] Here, the particle size of the hydrogen storage alloy particles is not particularly limited, but preferably, particles having a volume average particle size (MV) of 65.0 μm are used. In this disclosure, the volume average particle size (MV) refers to the volume average particle size determined by a laser diffraction / scattering method using a particle size distribution measurement device.

[0033] As the negative electrode additive, powder of a fluoride of a rare earth element (Sc, Y, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, and Lu) can be used. In this embodiment, yttrium fluoride (YF3) is used as the fluoride of a rare earth element. The amount of yttrium fluoride is preferably 0.1% by weight or more and 0.2% by weight, assuming that the weight of the hydrogen storage alloy powder is 100%. Furthermore, calcium fluoride may be added as the negative electrode additive.

[0034] The binder functions to bind the hydrogen storage alloy particles, the negative electrode additive, and the conductive material to one another, and also to bind the negative electrode mixture to the negative electrode core. Examples of the binder include hydrophilic or hydrophobic polymers. Examples of the conductive material include carbon black, graphite, and nickel powder.

[0035] To prepare a negative electrode mixture paste, 0.4 wt% sodium polyacrylate, 0.1 wt% carboxymethyl cellulose (CMC), 1.0 wt% styrene butadiene rubber (SBR) dispersion with a 50% solids content, 0.5 wt% Ketjen Black, 0.5 wt% calcium fluoride, 30 wt% ion-exchanged water, and a specified wt% yttrium fluoride were added and kneaded to 100% of the obtained hydrogen storage alloy powder. This paste was uniformly applied to both sides of the negative electrode core. After drying, the negative electrode core with the hydrogen storage alloy powder attached was further rolled to increase the amount of alloy per volume and cut to a specified size to produce a hydrogen storage alloy negative electrode. The negative electrode mixture not only filled the through-holes of the negative electrode core, but also formed layers on both sides of the negative electrode core.

[0036] The positive electrode 24 and negative electrode 26 produced in the above steps are wound up in a spiral shape with a separator 28 interposed between them, and then housed in an outer can 10. Then, a predetermined amount of electrolyte composed of a NaOH solution:LiOH solution in a weight ratio of 8.0:0.7 is poured into the outer can 10, and the opening of the outer can 10 is sealed. In this manner, a battery 2 with a nominal capacity of 2000 mAh is produced.

[0037] The fabricated battery 2 was subjected to an initial activation process by charging it at 0.20 A for 16 hours, then discharging it at 0.4 A until the battery voltage dropped to 1.0 V. This charge-discharge cycle was repeated five times to prepare the battery 2 for use.

[0038] 2. Working Example In order to investigate the cycle characteristics and low-temperature charging characteristics of the battery having the above configuration, the weight of the hydrogen storage alloy powder was set to 100 wt %, and the weight percentages of yttrium fluoride and calcium fluoride as negative electrode additives were changed to produce Battery 2. The production conditions for Battery 2 were all the same except for the amounts of yttrium fluoride and calcium fluoride added as negative electrode additives.

[0039] Example 1 A battery containing 0.2 wt % of yttrium fluoride as a negative electrode additive and no calcium fluoride was fabricated.

[0040] Example 2 A battery containing 0.2 wt % of yttrium fluoride and 0.5 wt % of calcium fluoride as negative electrode additives was fabricated.

[0041] Example 3 A battery containing 0.1 wt % of yttrium fluoride and 0.5 wt % of calcium fluoride as negative electrode additives was fabricated.

[0042] (Comparative Example 1) A battery was fabricated that did not contain either yttrium fluoride or calcium fluoride as a negative electrode additive.

[0043] (Comparative Example 2) A battery was fabricated that did not contain yttrium fluoride but contained 0.5 wt % of calcium fluoride as a negative electrode additive.

[0044] (Comparative Example 3) A battery containing 0.3 wt % of yttrium fluoride and 0.5 wt % of calcium fluoride as negative electrode additives was fabricated.

[0045] Comparative Example 4 A battery containing 0.05 wt % of yttrium fluoride and 0.5 wt % of calcium fluoride as negative electrode additives was fabricated.

[0046] 3. Evaluation of nickel-metal hydride secondary batteries (1) Low-temperature charging characteristics Each of the batteries of Examples 1 to 3 and Comparative Examples 1 to 4 that had undergone the initial activation treatment was (a) charged at 2.0 A in an environment of 25°C. At this time, charging was performed under so-called -ΔV control (hereinafter simply referred to as -ΔV charging), in which charging was terminated when the battery voltage reached its maximum value and then dropped 10 mV from this maximum value. After this -ΔV charging was completed, (b) the battery was left for one hour, and then discharged at 2.0 A until the battery voltage dropped to 1.0 V. The discharge capacity of Battery 2 at this time was measured and designated as the initial capacity [A] mAh. Then, (c) Battery 2 was left for one hour in an environment of 25°C. Three charge / discharge cycles were performed, with (a) to (c) constituting one cycle.

[0047] Next, Battery 2 was left in a 0°C environment for 3 hours, and then fully charged at 2.0 A in a 0°C environment, followed by -ΔV charging. After -ΔV charging in a 0°C environment, Battery 2 was left again in a 25°C environment for 3 hours, and then discharged at 2.0 A until the battery voltage dropped to 1.0 V. The discharge capacity of Battery 2 at this time was measured and designated as capacity [B] mAh. From the capacity obtained by the above procedure, the charge characteristic ratio was calculated using the following formula (I).

[0048] Low temperature charging characteristic ratio (%)=B / A=(capacity B) / (initial capacity A)...(I)

[0049] Therefore, the higher the low temperature charging characteristic ratio, the less the effect of a decrease in charging capacity due to low temperature (0° C.) when charging the battery 2 in an environment of 0° C. Figure 2 shows the low temperature charging characteristics of Examples 1 to 3 and Comparative Examples 1 to 3.

[0050] The low-temperature charging characteristics were 89.8% in Example 1, 92.2% in Example 2, and 92.7% in Example 3. In contrast, they were 88.5% in Comparative Example 1, 86.3% in Comparative Example 2, and 85.4% in Comparative Example 3.

[0051] Comparing the above results, it can be seen that the batteries of Examples 1 to 3 containing 0.1 wt% to 0.2 wt% yttrium fluoride have a higher discharge capacity after low-temperature charging than the batteries of Comparative Examples 1 to 3. This indicates that the capacity charged to the battery in a low-temperature environment, such as a 0°C environment, is large. It can also be seen that when the amount of yttrium fluoride is 0.05 wt%, less than 0.1 wt%, the low-temperature charging characteristics deteriorate, while when the amount of yttrium fluoride is 0.3 wt%, more than 0.2 wt%, the low-temperature charging characteristics deteriorate. Therefore, the low-temperature charging characteristics of the batteries containing 0.1 wt% to 0.2 wt% yttrium fluoride are excellent.

[0052] (2) Cycle life characteristics Each battery in Examples 1 to 3 and Comparative Examples 1 to 4 was charged at 1.0 C in a 25°C environment, and charging was terminated when the battery voltage dropped 10 mV from the maximum value, and the battery was left to stand for 1 hour. Subsequently, the battery was discharged at 1.0 C in the same environment until the battery voltage reached 1.0 V, and then the battery was left to stand for 1 hour. The above charge / discharge cycle constitutes one cycle, and charge / discharge was repeated, measuring the discharge capacity for each cycle. Here, the discharge capacity in the first cycle was taken as the initial capacity, and the capacity-to-initial ratio for each cycle was calculated using the following formula (II):

[0053] Capacity to initial ratio (%) = (discharge capacity at each cycle / initial capacity) × 100 (II)

[0054] Each battery in the Examples and Comparative Examples was repeatedly charged and discharged, and the number of cycles until the initial capacity ratio reached 60% was counted. The battery of Comparative Example 1, which did not contain either yttrium fluoride or calcium fluoride, was used as a standard product, and the cycle number of this standard product was set at 100. The ratio of the number of cycles for the batteries of Examples 1 to 3 and Comparative Examples 2 to 4 was calculated relative to the measured cycle number. The longer the number of cycles until the initial capacity ratio reached 60%, the longer the cycle life of the battery. This ratio is shown in Table 1 in FIG. 2.

[0055] The cycle life characteristics in Example 1 are 110In contrast, the values ​​were 103 in Comparative Example 2, 128 in Comparative Example 3, and 100 in Comparative Example 4.

[0056] From the above, as can be seen from Examples 1, 2, 3 and Comparative Example 3, by including 0.1 wt% or more of yttrium fluoride, the cycle life of the battery is extended compared to the batteries of Comparative Example 1 or Comparative Example 4 in which the yttrium fluoride content is less than 0.1 wt%.

[0057] Furthermore, when comparing Examples 1, 2, and 3, which contain 0.1 wt% or more of yttrium fluoride, it is found that the batteries of Examples 2 and 3, which contain calcium fluoride as an additive, have a longer cycle life than the battery of Example 1, which does not contain calcium fluoride. This tendency is also seen between the battery of Comparative Example 1, which does not contain either yttrium fluoride or calcium fluoride, and the battery of Comparative Example 2, which does not contain yttrium fluoride but does contain calcium fluoride. Thus, it is found that the battery to which calcium fluoride is added has a longer cycle life.

[0058] 4. Discussion The results in Table 1 show that batteries containing 0.1 to 0.2 wt% yttrium fluoride have improved low-temperature charging characteristics at temperatures such as 0°C compared to batteries containing no yttrium fluoride. Specifically, even in low-temperature environments, batteries containing 0.1 to 0.2 wt% yttrium fluoride can be charged to a capacity close to that at room temperature. This is thought to be because adding 0.1 to 0.2 wt% yttrium fluoride to the negative electrode mixture reduces factors that inhibit charging of the battery 2 in low-temperature environments and also enhances the corrosion-inhibiting effect of yttrium fluoride on the hydrogen storage alloy.

[0059] If the amount of yttrium fluoride added exceeds 0.2 wt%, the cycle life is extended but the low-temperature charging characteristics are degraded, and if the amount of yttrium fluoride added is less than 0.1 wt%, the absolute amount is considered to be insufficient to improve the low-temperature charging characteristics.

[0060] In addition, by comparing Example 1 with Example 2 or Comparative Example 1 with Comparative Example 2, it is clear that the cycle life of the battery containing calcium fluoride is longer than that of the battery containing no calcium fluoride.

[0061] Figure 3 shows a graph of the low-temperature charging characteristics and cycle life characteristics as a function of the amount of yttrium fluoride added, based on the results shown in Table 1. It can be seen that increasing the amount of yttrium fluoride added to the hydrogen storage alloy powder increases the cycle life. Meanwhile, the low-temperature charging characteristics peak between 0.1 and 0.2 wt% yttrium fluoride, and then decrease as the amount of yttrium fluoride increases.

[0062] From the above, it can be seen that by adding 0.1 wt % or more and 0.2 wt % or less of yttrium fluoride to the hydrogen storage alloy powder, as well as adding 0.5 wt % of calcium fluoride, it is possible to achieve both an extension of the cycle life of the nickel-metal hydride secondary battery and an improvement of the low-temperature charging characteristics.

[0063] The present invention is not limited to the above-described embodiments and examples, and various modifications are possible. For example, in addition to yttrium fluoride and calcium fluoride, fluorides of other rare earth elements can also be added as negative electrode additives. Furthermore, the nickel-metal hydride secondary battery may be a prismatic battery, and the shape of the battery is not particularly limited. [Explanation of symbols]

[0064] 2 Nickel-metal hydride secondary battery 24 Positive electrode 26 negative electrode 28 Separator

Claims

1. a hydrogen storage alloy; and yttrium fluoride as an additive, the mass of the yttrium fluoride is 0.1 parts by mass or more and 0.2 parts by mass or less per 100 parts by mass of the hydrogen storage alloy powder; The additive further contains calcium fluoride, A hydrogen storage alloy negative electrode, characterized in that the mass of the calcium fluoride is contained in an amount of 0.5 parts by mass or less relative to 100 parts by mass of the hydrogen storage alloy powder.

2. The hydrogen storage alloy negative electrode according to claim 1; a positive electrode containing nickel hydroxide, the positive electrode facing the hydrogen storage alloy negative electrode via a separator, The nickel-metal hydride secondary battery comprises the hydrogen storage alloy negative electrode and the positive electrode housed in an outer can together with an electrolyte.

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