JPS6110859A - Alkaline-zinc battery - Google Patents
Alkaline-zinc batteryInfo
- Publication number
- JPS6110859A JPS6110859A JP59104674A JP10467484A JPS6110859A JP S6110859 A JPS6110859 A JP S6110859A JP 59104674 A JP59104674 A JP 59104674A JP 10467484 A JP10467484 A JP 10467484A JP S6110859 A JPS6110859 A JP S6110859A
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- alkaline
- battery
- zinc alloy
- alloy powder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229910052725 zinc Inorganic materials 0.000 title claims description 27
- 239000011701 zinc Substances 0.000 title claims description 27
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 35
- 229910001297 Zn alloy Inorganic materials 0.000 claims description 33
- 239000000843 powder Substances 0.000 claims description 28
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 16
- 230000005484 gravity Effects 0.000 claims description 16
- 239000011787 zinc oxide Substances 0.000 claims description 8
- 239000007773 negative electrode material Substances 0.000 claims description 6
- 230000004907 flux Effects 0.000 claims 1
- 239000002245 particle Substances 0.000 description 51
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 13
- 239000003792 electrolyte Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 230000003647 oxidation Effects 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 238000000889 atomisation Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 230000008014 freezing Effects 0.000 description 4
- 238000007710 freezing Methods 0.000 description 4
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 4
- 239000002923 metal particle Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000011149 active material Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 230000010287 polarization Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 238000005275 alloying Methods 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000003349 gelling agent Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 229910001338 liquidmetal Inorganic materials 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 229960002523 mercuric chloride Drugs 0.000 description 2
- LWJROJCJINYWOX-UHFFFAOYSA-L mercury dichloride Chemical compound Cl[Hg]Cl LWJROJCJINYWOX-UHFFFAOYSA-L 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000000875 corresponding effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 229910052733 gallium Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229940008718 metallic mercury Drugs 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000007261 regionalization Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 229910001923 silver oxide Inorganic materials 0.000 description 1
- 229910000108 silver(I,III) oxide Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 229910002058 ternary alloy Inorganic materials 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/42—Alloys based on zinc
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
し発明の技術分野]
本発明は、アルカリ金属の水酸化物を主電解質とするア
ルカリ電解液中において、低汞化率または無水化で使用
する亜鉛負極に関するものである。[Detailed Description of the Invention] [Technical Field of the Invention] The present invention relates to a zinc negative electrode used in an alkaline electrolyte containing an alkali metal hydroxide as the main electrolyte with a low concentration ratio or in an anhydrous state. .
[発明の技術的背景]
一般にアルカリ電池用負極材料である亜鉛粉末ないし亜
鉛合金粉末は色々な方法でつくることができるが、最も
広く用いられているのは4N(純度 99.99%)以
上の高純度電気亜鉛を用い、アトマイズ法で噴霧して得
た不規則形状の粒子群からなる亜鉛粉末であって、粒径
(短径)60μmないし350 μm程度、形状指数
2.0 ないし2.3 程度、酸化亜鉛含有率0.
2 重量%ないし0.3 重石%程度のものである
。[Technical background of the invention] Zinc powder or zinc alloy powder, which is generally a negative electrode material for alkaline batteries, can be produced by various methods, but the most widely used method is 4N (purity 99.99%) or higher. Zinc powder consisting of a group of irregularly shaped particles obtained by atomizing high-purity electrolytic zinc using the atomization method, with a particle size (minor axis) of about 60 μm to 350 μm, and a shape index of 2.0 to 2.3. degree, zinc oxide content 0.
It is about 2% by weight to 0.3% by weight.
[背景技術の問題点コ
このような亜鉛粉末はアルカリ電解液中での水素過電圧
が低く、また実際上電解液量の極度に限定されている電
池内で放電された場合の化学分極も比較的大きいことか
ら、電池の種類・椛造や使用目的に応じて種々な程度に
氷化(amal(]amatiOn)して用いるのが普
通である。この場合の汞化率tよ、氷化亜鉛粉末バルク
の重量比として5 重量%ないし25重量%の範囲にあ
るが、特に6 重量%ないし12重量%稈度のものが多
用されている。[Problems in the background art] Such zinc powder has a low hydrogen overvoltage in an alkaline electrolyte, and also has a relatively low chemical polarization when discharged in a battery where the amount of electrolyte is actually extremely limited. Because of the large size of the battery, it is usually used after being frozen to various degrees depending on the type of battery, construction, and purpose of use.In this case, the freezing rate t is The weight ratio of the bulk is in the range of 5% to 25% by weight, and those having a culm of 6% to 12% by weight are particularly frequently used.
また、酸化亜鉛含有率は0.4 重量%ないし0.9
型間%程度のものが多い。In addition, the zinc oxide content is 0.4% by weight to 0.9% by weight.
In many cases, it is about % between molds.
負極中における多量の水銀の存在は、必然的に設計上電
池内で負極が占めるべく定められた容積内における活物
質量の減少をまねき電池容量の低下を伴なうから好まし
くない。のみならず周知のように水銀は公害規制物質で
あり、その使用量の低減は近年特に強い社会的要請とな
っている。負極亜鉛中の水銀添加量を低減するための研
究は広く行なわれてきており、その手段は主に化学的な
方法によるものが多く、例えば亜鉛合金組成、亜鉛粒子
の表面処理、アルカリ電解液への腐蝕抑制剤(l nh
ibitor)の添加等に関するものである。The presence of a large amount of mercury in the negative electrode is undesirable because it inevitably leads to a decrease in the amount of active material within the volume that the negative electrode is designed to occupy within the battery, resulting in a decrease in battery capacity. In addition, as is well known, mercury is a pollution control substance, and reducing its usage has become a particularly strong social demand in recent years. Research has been widely conducted to reduce the amount of mercury added in negative electrode zinc, and the methods for doing so are mainly chemical methods, such as zinc alloy composition, surface treatment of zinc particles, and changes in alkaline electrolyte. corrosion inhibitor (l nh
ibitor), etc.
このような目的の試みは研究的にはある程度の水準のも
のが得られつつあるが、亜鉛または亜鉛合金を粉末化し
無汞化の状態で、あるいは少なくとも従来に比して低い
汞化率で使用したときに従来の高い汞化率の氷化亜鉛粉
末に匹敵する程度の水素ガス発生抑制効果は得られてお
らず、商用アルカリ電池の負極活物質として実用化され
るに至っていない。Attempts for this purpose have been achieved to a certain degree in research, but zinc or zinc alloys are powdered and used in a non-oxidized state, or at least at a lower percentage of oxidation than in the past. However, it has not been found to be as effective in suppressing hydrogen gas generation as the conventional frozen zinc powder with a high degree of oxidation, and has not yet been put into practical use as a negative electrode active material for commercial alkaline batteries.
[発明の目的]
本発明の目的はアルカリ電池の負極に使用する亜鉛粉末
または亜鉛合金粉末の主として物理的性状の改良を行う
ことによって、従来技術のものに比して低汞化ないし無
汞化の状態で使用しても現用されている高い汞化率の氷
化亜鉛粉末に匹敵する程度に電池内での水素ガス発生が
少なく、従って貯蔵特性のよいアルカリ・亜鉛電池を提
供することである。[Objective of the Invention] The object of the present invention is to improve the physical properties of zinc powder or zinc alloy powder used in the negative electrode of alkaline batteries, thereby making the zinc powder or zinc alloy powder lower or less resistant than those of the prior art. To provide an alkaline-zinc battery that generates as little hydrogen gas within the battery as the currently used frozen zinc powder with a high degree of oxidation even when used under conditions of .
[発明の概要コ
即ち本発明では不可避的混入元素、特に鉄含有率の可及
的少ない高純度亜鉛または亜鉛に少量添加して合金化せ
しめることにより、アルカリ電解液中で防蝕効果をもた
らし、且つ分極特性を阻害することのない金属性元素を
添加した亜鉛合金を用い、且つ該亜鉛または亜鉛合金を
実用上の所定粒度ないし平均粒径となるよう粒状化する
に際して、従来品に比較してカサ比重を著しく大きくす
るようにした噴霧亜鉛合金粉末をアルカリ電池の負極活
物質として使用することによって、従来品に比して低い
汞化率ないし無汞化で使用した場合にも電池内にお(〕
る水素ガス発生を実用上充分な程度にまで抑制できるよ
うにしたものである。[Summary of the Invention] In other words, in the present invention, by adding a small amount to high-purity zinc or zinc with an unavoidable contamination element, especially iron content as low as possible, and alloying it, a corrosion-preventing effect is brought about in an alkaline electrolyte, and When using a zinc alloy to which metallic elements are added that do not inhibit polarization characteristics, and when granulating the zinc or zinc alloy to a practical predetermined particle size or average particle size, it is bulkier than conventional products. By using atomized zinc alloy powder with a significantly increased specific gravity as the negative electrode active material of alkaline batteries, even when used at a lower rate of oxidation or no oxidation compared to conventional products, the ( ]
This makes it possible to suppress hydrogen gas generation to a practically sufficient level.
[弁明の実施例] 以下実施例を用いて本発明の詳細な説明する。[Example of explanation] The present invention will be described in detail below using Examples.
第1表に本発明による噴霧亜鉛合金粉末と従来技術によ
る噴霧亜鉛合金粉末とのアルカリ電解液中における水素
ガス発生速度、カサ比重、平均形状指数及び酸化亜鉛含
有率の比較を示した。第1表において水素ガス発生速度
は、酸化亜鉛を飽和した35%KOH溶液10 m体
中に 10 (lの被験試料を浸漬し、数torrの減
圧下で30分間脱気したのち、電解液面を流動パラフィ
ンで充し、60℃で174時間放置したときのものであ
る。また平均形状指数は、各粒子の最大方向の長さを休
(長径)、シ軸と直角方向の最も大きい長さをS(短径
)としたときi/sは、即ちその粒子の変形度を細長さ
で現わした形状指数である。実用されているアトマイズ
亜鉛粉末はさまざまな形状のものを含んでおり、これら
粒子の変形度を示すのに平均形状指数を用いるのが最も
簡明且つ実用的である。一般に多用される噴霧亜鉛粒子
の形状指数は大部分が1,8 ないし3.6 程度
のものであり、その平均的形状指数は2.0 ないし
2.3 程度である。Table 1 shows a comparison of the hydrogen gas generation rate, bulk specific gravity, average shape index, and zinc oxide content in an alkaline electrolyte between the sprayed zinc alloy powder according to the present invention and the sprayed zinc alloy powder according to the prior art. In Table 1, the hydrogen gas generation rate is determined by immersing 10 (l) of the test sample in 10 m of a 35% KOH solution saturated with zinc oxide, degassing it for 30 minutes under a reduced pressure of several torr, and then Filled with liquid paraffin and left at 60°C for 174 hours.The average shape index is the length of each particle in the maximum direction (major axis), and the maximum length in the direction perpendicular to the axis. When S (minor axis) is defined as S (minor axis), i/s is the shape index that expresses the degree of deformation of the particle in terms of slenderness.Practical atomized zinc powder includes a variety of shapes. It is simplest and most practical to use the average shape index to indicate the degree of deformation of these particles.The shape index of the commonly used atomized zinc particles is mostly around 1.8 to 3.6. , its average shape index is about 2.0 to 2.3.
ある粉末を標準篩とS盪機を用いて分級して示される粒
度ないし粒度分布とは、その分級条件が妥当であれば略
々上述した短径(S)の粒径ないし粒径分布を示すもの
である。The particle size or particle size distribution shown by classifying a certain powder using a standard sieve and an S shaker is approximately the particle size or particle size distribution of the short diameter (S) described above if the classification conditions are appropriate. It is something.
第1表
第1表中り、Eは本発明の実施例、Aは従来例、B、C
は比較例である。即ち第1表中Aは代表的従来品であっ
て、純度4Nの電気亜鉛を大気中でアトマイズ法により
粒状化したのち、100μmないし 300μmの範囲
に分級し、稀Na OH溶液中で金属水銀と氷化せしめ
て得た汞化率6.5 重量%の氷化亜鉛粉末である。Table 1 In Table 1, E is an example of the present invention, A is a conventional example, B, C
is a comparative example. That is, A in Table 1 is a typical conventional product, in which electrolytic zinc with a purity of 4N is granulated by the atomization method in the air, then classified into particles in the range of 100 μm to 300 μm, and mixed with metallic mercury in a dilute NaOH solution. This is frozen zinc powder with a viscosity of 6.5% by weight.
このものの氷化前(未氷化)のカサ比重は普通2.5
g −cnr3ないし2.8g・cm−3程度のもので
ある。The bulk specific gravity of this thing before freezing (unfrozen) is usually 2.5.
g-cnr3 to about 2.8 gcm-3.
次に第1表中Bは比較量であって同様に純度4Nの電気
亜鉛を大気中でアトマイズ法により粒状化し、分級後、
所要量の塩化第二水銀を含む稀CH3C0OH溶液中文
処理し、氷化せしめて得た汞化率2.81重量%の低汞
化亜鉛合金粉末である。Next, B in Table 1 is a comparative amount, in which electrolytic zinc with a purity of 4N was granulated by the atomization method in the air, and after classification,
This is a low filtration zinc alloy powder with a filtration rate of 2.81% by weight, obtained by treating a dilute CH3C0OH solution containing the required amount of mercuric chloride and freezing it.
第1表中Cも比較量であって!10.15重量%、ガリ
ウム0.13重量%を含む亜鉛合金を大気中でアトマイ
ズ法で粒状化したのち、100μmないし300μmの
範囲に分級して得た無汞化亜鉛合金粉末である。C in Table 1 is also a comparative amount! This is an amorphous zinc alloy powder obtained by atomizing a zinc alloy containing 10.15% by weight and 0.13% by weight of gallium in the air by an atomizing method, and then classifying the powder into particles in the range of 100 μm to 300 μm.
第1表中りないしEは、それぞれ本発明の一実施例であ
って、Dは前記Bと同様純度4Nの電気亜鉛を窒素雰囲
気中でアトマイズ法により粒状化したのべ分級して粒径
100μmないし300μmとし、次に所要量の塩化
第二水銀を含む稀CH3CO0H溶液中で処理して得た
汞化率2.85重量%の低汞化亜鉛合金粉末である。ま
たEは前記Cと同一組成のZn −Rb−Ga三元合金
を窒素ガス雰囲気中でアトマイズ法により粒状化したの
ち分級して粒径100 μmないし300 μmの
範囲とした無汞化亜鉛合金粉末である。In Table 1, E to E are examples of the present invention, and D is the same as B above, granulated electrolytic zinc with a purity of 4N by the atomization method in a nitrogen atmosphere and classified to have a particle size of 100 μm. to 300 μm, and then treated in a dilute CH3CO0H solution containing the required amount of mercuric chloride. This is a low filtration zinc alloy powder with a filtration rate of 2.85% by weight. Further, E is a non-aqueous zinc alloy powder which is made by granulating a Zn-Rb-Ga ternary alloy having the same composition as C above by an atomizing method in a nitrogen gas atmosphere, and then classifying the powder to have a particle size in the range of 100 μm to 300 μm. It is.
第1表り、Eで示した本発明のカサ比重を大きくするよ
うにした亜鉛合金粉末の場合には、2.85重量%の低
水化率ないし無汞化で用いてもカサ比重の小さいB、C
に比べ水素ガス発生速度が著しく減少していることがわ
かる。また、Eはこれを1ないし3重量%低永化率に氷
化することによって、水素ガス発生速度を更に小さくす
ることができる。In the case of the zinc alloy powder of the present invention, which has a high bulk specific gravity as indicated by E in Table 1, the bulk specific gravity is small even when it is used with a low water conversion rate of 2.85% by weight or with no water content. B, C
It can be seen that the hydrogen gas generation rate is significantly reduced compared to the above. Furthermore, E can further reduce the rate of hydrogen gas generation by freezing it to a low aging rate of 1 to 3% by weight.
本発明におけるカサ比重の大きい亜鉛合金粒が略々同一
粒度においてアルカリ電解液中で水素ガス発生の少ない
理由については、充分解明できていない。しかしながら
SEMによれば図面に示したような粒子形状の差が観察
される。第1図に本発明による噴霧亜鉛合金粉末の粒子
形状モデルを示し、第2図には従来粉末の粒子形状モデ
ルを示した。各図とも(a>は粒径の大きいもの、(b
)は短径の小さいものの形状モデルである。第1図に示
した本発明の亜鉛合金粒では、第2図に示した従来品に
比して粒子形状に鋭角的な部分が著しく少なく粒子端部
が全体に丸味を帯びており、粒子表面にもシワ状模様の
形成がほとんどみられない。The reason why the zinc alloy particles having a large bulk specific gravity in the present invention generate less hydrogen gas in an alkaline electrolyte when the particle size is substantially the same has not been fully elucidated. However, according to SEM, differences in particle shape as shown in the drawings are observed. FIG. 1 shows a particle shape model of the atomized zinc alloy powder according to the present invention, and FIG. 2 shows a particle shape model of the conventional powder. In each figure, (a> is the one with a large particle size, (b
) is a shape model with a small short axis. The zinc alloy grains of the present invention shown in Fig. 1 have significantly fewer sharp angles in the particle shape than the conventional product shown in Fig. 2, and the particle ends are rounded as a whole, and the particle surface There is hardly any wrinkle-like pattern formation on the surface.
また、粒径の小さい粒子はど従来品に比して一層球体に
近く、形状指数1.0 に近いものが多く混在してい
る。またこの形状変化に対応して平均粒状指数も従来の
2.0 ないし2.3 程度に対し、本発明の場合
は1.8 以下となっている。これらの形状変化はカ
サ比重を大きくしている主因と考えられるが、同時に粒
子間の摩擦を少なくしブリッジも形成し難いため粉体流
動性(flow rate )も改良されていることが
認められている。In addition, the particles with small particle diameters are more similar to spheres than the conventional products, and there are many particles with a shape index close to 1.0. Corresponding to this change in shape, the average graininess index is also 1.8 or less in the case of the present invention, compared to about 2.0 to 2.3 in the conventional case. These changes in shape are thought to be the main reason for increasing the bulk specific gravity, but at the same time, it has been recognized that the powder flow rate is also improved because it reduces friction between particles and makes it difficult to form bridges. There is.
また、第1表に示したよう・にカサ比重の大きい亜鉛合
金粉末では酸化亜鉛含有率が著しく小さい。Furthermore, as shown in Table 1, zinc alloy powders with large bulk specific gravity have a significantly low zinc oxide content.
酸化亜鉛含有率は過大でなければ水素ガス発生速度にそ
れほど影響しないが、水素ガス発生量のバラツキを生じ
やすく、特にアルカリ電池に実用する場合苛酷な使用条
件下の特性、例えば低温における急放電特性やパルス放
電特性を低丁させることがある。The zinc oxide content does not significantly affect the hydrogen gas generation rate if it is not excessive, but it tends to cause variations in the amount of hydrogen gas generated, and especially when used in alkaline batteries, the characteristics under harsh usage conditions, such as rapid discharge characteristics at low temperatures. This may cause the pulse discharge characteristics to deteriorate.
また、酸化亜鉛は電池の反応生成物であり、その過度の
含有は活物質量の減少を意味するから、その含有率は可
及的に小さいことが望ましい。Furthermore, since zinc oxide is a reaction product of batteries, and its excessive content means a decrease in the amount of active material, it is desirable that its content be as small as possible.
[発明の効果]
以上の観察から本発明の効果について次の如く考察され
るっすなわち過度現象的にみると従来における場合は、
ノズルから圧出された溶融亜鉛ないし溶融亜鉛合金がエ
アー・ブローによって噴霧化された直後の清浄な液滴状
金属粒子表面に急速に単分子層またそれ以上の厚さの酸
化膜が生成される。酸化膜の生成は液状金属粒子の界面
張力を変化させ、個々の粒子形状が界面張力による凝集
の影響を充分うけないうちに融点以下にまで冷却固化し
てしまうため、粒子の大きさに応じ噴n@の加速度・方
向や重力等によって支配されるさまざまな不規則形状の
粒子を生じ、且つ粒子端部に鋭角的部分が形成され易い
のである。また金属粒子表面のシワ状模様の形成は、表
面に酸化膜の生成した液状金属粒子が冷部固化するまで
の運動の過程で刻々形状変化をし、その都度表面の硬化
膜が破れて新鮮な金属面が露出し、その部分が再酸化す
るということの繰返しによって生成されたものと考えら
れる。[Effects of the Invention] From the above observations, the effects of the present invention can be considered as follows. In other words, from a transient phenomenon perspective, in the conventional case,
Immediately after the molten zinc or molten zinc alloy extruded from the nozzle is atomized by air blowing, an oxide film of a monomolecular layer or thicker is rapidly formed on the surface of the clean droplet-shaped metal particles. . The formation of an oxide film changes the interfacial tension of liquid metal particles, and the shape of each particle cools to below the melting point and solidifies before it is sufficiently affected by agglomeration due to the interfacial tension. Particles with various irregular shapes are produced depending on the acceleration/direction of n@, gravity, etc., and sharp parts are likely to be formed at the ends of the particles. In addition, the formation of wrinkle-like patterns on the surface of metal particles occurs because liquid metal particles with an oxide film formed on the surface change shape every moment as they move until they solidify in the cold. It is thought that the metal surface was exposed and that part was repeatedly oxidized.
これに対して本発明の実施例1で示した場合には、ノズ
ルから圧出された溶融亜鉛または溶融亜鉛合金が高圧窒
素ガスで不活性ガス雰囲気中へ噴霧され、粒状化された
ときに液状合金粒子表面がほとんどまたは全く酸化を受
けないので、界面張力による凝集2球状化の作用を受は
易く、また粒子が融点以下に冷却固化するまでの間に加
速度や重力の影響を受けることの小さい微粒子はど球状
化し易いものと考えられる。On the other hand, in the case shown in Example 1 of the present invention, molten zinc or molten zinc alloy pressed out from a nozzle is sprayed into an inert gas atmosphere with high-pressure nitrogen gas, and when granulated, it becomes a liquid. Since the alloy particle surface undergoes little or no oxidation, it is easily susceptible to the effects of agglomeration and spheroidization due to interfacial tension, and is less affected by acceleration and gravity until the particles are cooled below their melting point and solidified. It is thought that fine particles are easily spherical.
半径の大きい粒子では重力等の影響により粒子形状全体
としては球状化し難く不規則形状になり易いけれども、
局部的には粒子の端部が丸味を帯び鋭角的な部分が減少
するので形状指数は小となる。また粒子表面は酸化膜の
影響を受けないので比較的平滑面となる。これらの結果
から平均形状指数が小さくなり、粒子間の摩擦が減少し
て流動性をよくし、カサ比重を大きくしているものと思
われる。またこれら°の変化が合金結晶や結晶粒界の状
態および粒界への不可避的含有不純元素や有効添加元素
の偏析挙動に何らかの変化をもたらし、結果的に本発明
による噴霧亜鉛合金粉末の水素過電圧を大きくしている
ものと思われる。いずれにしてもこのような好ましい特
性上の変化は、カサ比重の変化と相関対応していること
によって、カサ比重によって一括管理することが可能で
あることがわかった。For particles with a large radius, it is difficult for the particle shape to become spherical as a whole due to the influence of gravity, etc., and it is easy to become irregular in shape.
Locally, the edges of the particles become rounded and the sharp angles are reduced, so the shape index becomes small. Furthermore, the particle surface is not affected by the oxide film, so it becomes a relatively smooth surface. From these results, it seems that the average shape index becomes smaller, the friction between particles decreases, improving fluidity and increasing the bulk specific gravity. In addition, these changes bring about some changes in the state of alloy crystals and grain boundaries, as well as in the segregation behavior of unavoidably contained impurity elements and effective additive elements in grain boundaries, and as a result, the hydrogen overvoltage of the sprayed zinc alloy powder according to the present invention changes. It seems that it is making the . In any case, it has been found that such changes in preferable characteristics are correlated with changes in bulk specific gravity, and can therefore be collectively managed based on bulk specific gravity.
以−トのごとく本発明は高純度亜鉛または亜鉛に少量添
加して合金化せしめることによりアルカリ電解液中で防
蝕効果をもたらし、且つ分極特性を阻害づることのない
金属性元素を添加した亜鉛合金を用い、且つ該亜鉛また
は亜鉛合金を実用上の所定粒度ないし平均粒径となるよ
う粒状化するに際して、従来品に比してカサ比重を著し
く大きくするようにした亜鉛粉末ないし亜鉛合金粉末を
アルカリ電池の負極活物質として使用することによって
、従来に比して低い汞化率ないし無汞化で使用した場合
にも電池内における水素ガス発生を相当程度抑制できる
ようにしたものである。また、このようにカサ密度の大
きい粉末を用いることによつC同一負極容積における活
物質量を増大せしめ、低温における急放電特性を向上で
きると共に電池の製造工程においても、取扱作業性がよ
く容積計量時における電池内充填重量のバラツキの少な
いゲル状亜鉛負極を得ることができる等、その工業的効
果の大きいものである。As described above, the present invention provides high purity zinc or a zinc alloy to which a metallic element is added which provides a corrosion-proofing effect in an alkaline electrolyte by adding a small amount to zinc and alloying it, and which does not impede the polarization characteristics. When granulating the zinc or zinc alloy to a practical predetermined particle size or average particle size, the zinc powder or zinc alloy powder whose bulk specific gravity is significantly larger than that of conventional products is treated with an alkali. By using it as a negative electrode active material in a battery, it is possible to suppress the generation of hydrogen gas within the battery to a considerable extent even when the battery is used at a lower rate of oxidation or no oxidation than before. In addition, by using a powder with a large bulk density, the amount of active material can be increased in the same C negative electrode volume, improving rapid discharge characteristics at low temperatures, and improving handling workability in the battery manufacturing process. This method has great industrial effects, such as being able to obtain a gelled zinc negative electrode with little variation in the weight filled in the battery during measurement.
本発明による低汞化ないし無汞化の亜鉛合金粉末はアル
カリ電解液及び任意のゲル化剤と混合したゲル状亜鉛を
負極に用いるいわゆるゲル方式及び亜鉛合金粒子表面に
あらかじめ主としてゲル化剤からなる71I層を形成せ
しめておき、これを負極容器内でアルカリ電解液の注入
によりゲル化させるいわゆるPowder with
Gel方式の何れにも適用できる。The zinc alloy powder of the present invention which has low or no gradient has a so-called gel method in which a gelled zinc mixed with an alkaline electrolyte and an arbitrary gelling agent is used as a negative electrode, and a gelling agent is mainly provided on the surface of the zinc alloy particles. 71I layer is formed in advance, and this is gelled by injecting an alkaline electrolyte in the negative electrode container, so-called Powder with.
It can be applied to any Gel method.
また本発明の技術は過酸化銀電池、酸化銀電池。The technology of the present invention also applies to silver peroxide batteries and silver oxide batteries.
ニッケル・亜鉛電池、アルカリ・マンガン電池。Nickel/zinc batteries, alkaline/manganese batteries.
空気・亜鉛電池等亜鉛を負極活物質とする各種構造(円
筒型、ボタン型、コイン型、超扁平型等)のアルカリ電
池に適用して効果を発揮するものである。It is effective when applied to alkaline batteries of various structures (cylindrical, button, coin, ultra-flat, etc.) that use zinc as the negative electrode active material, such as air-zinc batteries.
第1図は本発明の噴霧亜鉛粉末を構成する粒子の粒子形
状モデルであり、第2図は従来の噴霧亜鉛合金粉末を構
成する粒子の粒子形状モデルである。各図ども(a7は
粒径の大きいもの、(b)は粒径の小さいものの粒子形
状を示す。
第1図 第2図
(Q)(η)
(b) Cb)手続補正鋼(
方式)
%式%
1、 事件の表示
昭和59年特許願第104674号
2、 発明の名称
アルカリ・亜鉛電池
3、 補正をする者
事件との関係 特許出願人
〒14g
シナガワグミナミシナガワ
住 所 東京部品用区南品用3丁目4番10号トウシバ
ゾンデ −
名称(353)東芝電池株式会社
4、 補正命令の日付
昭和59年8月8日FIG. 1 is a particle shape model of particles constituting the atomized zinc powder of the present invention, and FIG. 2 is a particle shape model of particles constituting the conventional atomized zinc alloy powder. Each figure (a7 shows the particle shape of a large particle size, (b) shows the particle shape of a small particle size. Figure 1 Figure 2 (Q) (η) (b) Cb) Procedure correction steel (
Method) % formula % 1, Indication of the case Patent Application No. 104674 of 1982 2, Name of the invention Alkaline Zinc Battery 3, Relationship with the person making the amendment Patent applicant address 14g Shinagawa Gminami Shinagawa Address Tokyo Parts Toshibasonde No. 3-4-10 Minamishina - Name (353) Toshiba Battery Co., Ltd. 4 Date of amendment order August 8, 1980
Claims (2)
電池において、該亜鉛合金粉末の汞化率が3重量%以下
、酸化亜鉛含有率が0.3重量%以下で且つカサ比重が
3.4g・cm^−^3以上である低汞化ないし無汞化
の亜鉛合金粉末を用いることを特徴とするアルカリ・亜
鉛電池。(1) In an alkaline battery using zinc alloy powder as the negative electrode active material, the zinc alloy powder has a viscosity rate of 3% by weight or less, a zinc oxide content of 0.3% by weight or less, and a bulk specific gravity of 3.4g. An alkaline zinc battery characterized in that it uses a zinc alloy powder with low or zero flux of at least cm^-^3.
ることを特徴とする特許請求の範囲第1項記載のアルカ
リ・亜鉛電池。(2) The alkaline zinc battery according to claim 1, wherein the zinc alloy powder has an average shape index of 1.8 or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59104674A JPS6110859A (en) | 1984-05-25 | 1984-05-25 | Alkaline-zinc battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59104674A JPS6110859A (en) | 1984-05-25 | 1984-05-25 | Alkaline-zinc battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6110859A true JPS6110859A (en) | 1986-01-18 |
| JPH0348618B2 JPH0348618B2 (en) | 1991-07-25 |
Family
ID=14387016
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59104674A Granted JPS6110859A (en) | 1984-05-25 | 1984-05-25 | Alkaline-zinc battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6110859A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006228503A (en) * | 2005-02-16 | 2006-08-31 | Sony Corp | Alkaline battery |
| JP2015106449A (en) * | 2013-11-28 | 2015-06-08 | Dowaホールディングス株式会社 | Zinc alloy powder for alkali batteries and manufacturing method thereof, and alkali battery arranged by use thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5498937A (en) * | 1978-01-20 | 1979-08-04 | Matsushita Electric Industrial Co Ltd | Alkaline cell |
| JPS56147364A (en) * | 1980-04-16 | 1981-11-16 | Matsushita Electric Ind Co Ltd | Preparation of amalgamed zinc powder |
| JPS58218762A (en) * | 1982-06-11 | 1983-12-20 | Toshiba Battery Co Ltd | Alkaline battery |
| JPS5925168A (en) * | 1982-08-04 | 1984-02-09 | Fuji Elelctrochem Co Ltd | Enclosed alkaline battery |
-
1984
- 1984-05-25 JP JP59104674A patent/JPS6110859A/en active Granted
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5498937A (en) * | 1978-01-20 | 1979-08-04 | Matsushita Electric Industrial Co Ltd | Alkaline cell |
| JPS56147364A (en) * | 1980-04-16 | 1981-11-16 | Matsushita Electric Ind Co Ltd | Preparation of amalgamed zinc powder |
| JPS58218762A (en) * | 1982-06-11 | 1983-12-20 | Toshiba Battery Co Ltd | Alkaline battery |
| JPS5925168A (en) * | 1982-08-04 | 1984-02-09 | Fuji Elelctrochem Co Ltd | Enclosed alkaline battery |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006228503A (en) * | 2005-02-16 | 2006-08-31 | Sony Corp | Alkaline battery |
| JP2015106449A (en) * | 2013-11-28 | 2015-06-08 | Dowaホールディングス株式会社 | Zinc alloy powder for alkali batteries and manufacturing method thereof, and alkali battery arranged by use thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0348618B2 (en) | 1991-07-25 |
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