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JPH0348619B2 - - Google Patents
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JPH0348619B2 - - Google Patents

Info

Publication number
JPH0348619B2
JPH0348619B2 JP59104675A JP10467584A JPH0348619B2 JP H0348619 B2 JPH0348619 B2 JP H0348619B2 JP 59104675 A JP59104675 A JP 59104675A JP 10467584 A JP10467584 A JP 10467584A JP H0348619 B2 JPH0348619 B2 JP H0348619B2
Authority
JP
Japan
Prior art keywords
zinc
powder
particle
particles
weight
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.)
Expired - Lifetime
Application number
JP59104675A
Other languages
Japanese (ja)
Other versions
JPS6110860A (en
Inventor
Akira Hayashi
Kazumasa Yoshida
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FDK Twicell Co Ltd
Original Assignee
Toshiba Battery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toshiba Battery Co Ltd filed Critical Toshiba Battery Co Ltd
Priority to JP59104675A priority Critical patent/JPS6110860A/en
Publication of JPS6110860A publication Critical patent/JPS6110860A/en
Publication of JPH0348619B2 publication Critical patent/JPH0348619B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/42Alloys based on zinc
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy 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)

Description

【発明の詳細な説明】[Detailed description of the invention]

[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
無汞化で使用する亜鉛負極に関するものである。 [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
なる亜鉛粉末であつて、粒径(短径)60μmない
し350μm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重量%程度のもの
である。 [背景技術の問題点] 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・構造や使
用目的に応じて種々な程度に汞化
(amalgamation)して用いるのが普通である。
この場合の汞化率は、汞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%程度のものが多
用されている。また、酸化亜鉛含有率は0.4重量
%ないし0.9重量%程度のものが多い。 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つている。 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、その改善手段として
は主に亜鉛合金組成、亜鉛粒子の表面処理、アル
カリ電解液への腐蝕抑制剤(Inhibitor)の添加
に関するものである。なかでも最も基本的な手段
の一つは、亜鉛と合金化せしめることによつてそ
の水素過電圧を高め且つ放電特性を阻害すること
のない第三金属元素の添加であり、このような有
効添加元素として提案されているもののほとんど
は周期律表第b族、第b族、第b族、第
b族、第b族に属する金属性元素である。 このような目的の亜鉛合金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、これらの亜
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汞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てい
ない。 [発明の目的] 本発明の主たる目的はアルカリ電池の負極亜鉛
粉末または亜鉛合金粉末の化学組成と物理的性状
の両側面から改良を行うことによつて、従来技術
のものに比して著しく低汞化率ないし無汞化の状
態で使用しても現用されている高い汞化率の汞化
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、従つ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。 [発明の概要] 即ち本発明の方法で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
ない複数種の金属性元素を添加した亜鉛合金を用
い、且つ該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つて、従来品に比して著し
く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。 [発明の実施例] 以下実施例を用いて本発明の詳細を説明する。
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10ml中に10g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
液面を流動パラフインで充し、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l(長径)、l軸と直角
方向の最も大きい長さをs(短径)としたとき
l/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
される噴霧亜鉛粒の形状指数は大部分の粒子が
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。ある粉末を標準
篩と振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。
[Technical Field of the Invention] The present invention relates to a zinc negative electrode that is used at a low or zero rate in an alkaline electrolyte containing an alkali metal hydroxide as the main electrolyte. [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 is 4N (purity
Zinc powder consisting of a group of irregularly shaped particles obtained by atomizing using high-purity electrolytic zinc (99.99%) or higher, with a particle diameter (minor axis) of about 60 μm to 350 μm, and a shape index of 2.0 to 2.3. The zinc oxide content is about 0.2% to 0.3% by weight. [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 their large size, they are usually amalgamated to various degrees depending on the type, structure, and intended use of the battery.
In this case, the filtration rate is in the range of 5% to 25% by weight as a weight ratio of the bulk zinc filtrate powder, and in particular, a ratio of 6% to 12% by weight is often used. Further, the zinc oxide content is often about 0.4% by weight to 0.9% by weight. 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. Furthermore, 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 main methods of improvement include zinc alloy composition, surface treatment of zinc particles, and addition of corrosion inhibitors to alkaline electrolytes. It is about addition. Among these, one of the most basic methods is the addition of a third metal element that increases the hydrogen overvoltage by alloying with zinc and does not impede the discharge characteristics. Most of the elements proposed as such are metallic elements belonging to groups b, b, b, b, b, and b of the periodic table. Zinc alloys for this purpose are being obtained to a certain level through research, but these zinc alloys cannot be pulverized and made into a non-oxidized state, or at least with a lower percentage of oxidation than before. When used, it has not been found to have a hydrogen gas generation suppressing effect comparable to that of conventional zinc oxide powder with a high oxidation rate, and has not been put to practical use as a negative electrode active material for commercial alkaline batteries. [Objective of the Invention] The main object of the present invention is to improve the chemical composition and physical properties of negative electrode zinc powder or zinc alloy powder for alkaline batteries, thereby achieving significantly lower levels than those of the prior art. Even if it is used in a state of oxidation or no oxidation, it generates less hydrogen gas in the battery to the extent that it is comparable to the currently used zinc powder with a high oxidation ratio, and therefore has good storage characteristics. It is to provide a zinc battery. [Summary of the invention] That is, in the method of the present invention, by adding a small amount to zinc and alloying it, multiple types of metallic elements are added that provide a corrosion-preventing effect in an alkaline electrolyte and do not impede the polarization characteristics. When granulating the zinc alloy to a predetermined practical particle size or an average particle size, the atomized zinc alloy powder has a significantly larger bulk specific gravity than conventional products, and is used in alkaline batteries. By using it as a negative electrode active material, hydrogen gas generation within the battery can be suppressed to a practically sufficient level even when used at a significantly lower rate of oxidation or no oxidation compared to conventional products. This is what I did. [Examples of the Invention] The details of the present invention will be explained below using Examples.
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 g of the test sample in 10 ml of a 35% KOH solution saturated with zinc oxide, degassing it for 30 minutes under a reduced pressure of several torr, and then cleaning the electrolyte surface with liquid paraffin. This is when the sample was filled and left at 60℃ for 174 hours. Also, the average shape index is
When the length of each particle in the maximum direction is l (major axis) and the maximum length in the direction perpendicular to the l axis is s (minor axis), l/s expresses the deformation degree of the particle in terms of slenderness. This is the shape index. Atomized zinc powder in practical use includes various 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 that most of the particles are
The average shape index is about 1.8 to 3.6, and the average shape index is about 2.0 to 2.3. The particle size or particle size distribution shown by classifying a certain powder using a standard sieve and a shaker is approximately the particle size or particle size distribution of the short diameter s described above, if the classification conditions are appropriate. .

【表】 第1表中D、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
表的従来品であつて、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、100μ
mないし300μmの範囲に分級し、稀NaOH溶液
中で金属水銀と汞化せしめて得た汞化率6.5重量
%の汞化噴霧亜鉛粉末である。このもののカサ比
重は3.12g・cm-3とやや大きくなつているが、こ
れは高い水銀含有量によつて真比重が大きくなつ
ているためであつて、汞化前(未汞化)のカサ比
重は普通2.5g・cm-3ないし2.8g・cm-3程度のも
のである。 次に第1表中Bは比較品であつて鉛0.20重量
%、ガリウム0.18重量%、錫0.06重量%を含む亜
鉛合金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
CH3COOH溶液中で処理し、汞化せしめて得た
汞化率1.37重量%の低汞化噴霧亜鉛合金粉末であ
る。第1表中Cも比較品であつて鉛0.15重量%、
ガリウム0.13重量%、インジウム0.025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
得た無汞化噴霧亜鉛合金粉末である。 第1表中D及びEは、それぞれ本発明の一実施
例であつて、Dは前記Bと同一組成のZn−Pb−
Ga−Sn系四元合金を窒素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100μmな
いし300μmとし、次に所要量の塩化第二水銀を
含む稀CH3COOH溶液中で処理して得た汞化率
1.34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−Pb−Ga−In系四元合
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系100μmないし300μmの
範囲とした無汞化噴霧亜鉛合金粉末である。 第1表B、Cの水素ガス発生速度から判るよう
に、周期律表第b族、第b族、第b族、第
b族、第b族に属する元素の群から選択した
複数金属性元素を効果的に組合せて添加した噴霧
亜鉛合金粉末は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、それ自体水素ガス発
生は非常に減少する。すなわち純度4Nの電気亜
鉛から同様に製した噴霧亜鉛粉末では、例えば無
汞化の場合試験温度45℃においても第1表Cの60
℃における値の数十倍の水素ガス発生速度を示す
からである。 しかしながら第1表Aに示した高い汞化率の従
来品に比べるとなお水素ガス発生量が多いことが
判る。これに対して第1表D、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噴霧合金
粉末の場合には、1.34重量%の低汞化率ないし無
汞化で用いても前記B、Cに比べて水素ガス発生
速度が半減し高い汞化率の従来例Aに近い値を示
していることが判る。 本発明におけるカサ比重の大きい噴霧亜鉛合金
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
した本発明の噴霧亜鉛合金粒では、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。 また、粒径の小さい粒子ほ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1.6〜1.0となつている。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ツジも形
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。 また、第1表に示したようにカサ比重の大きい
噴霧亜鉛合金粉末では酸化亜鉛含有率が著しく小
さい。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下さ
せることがある。 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。 [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。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・ブローによつて噴霧
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霧時
の加速度・方向や重力等によつて支配されるさま
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却固化するまでの運動の
過程で刻々形状変化をし、その都度表面の酸化膜
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つて生成されたも
のと考えられる。 これに対して本発明の実施例で示した場合に
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・球状化の作用を受け易く、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ほど球状
化し易いものと考えられる。 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つ
て、カサ比重によつて一括管理することが可能で
あることがわかつた。 以上のごとく本発明は亜鉛―鉛―ガリウムの三
元合金に、錫もしくはインジウムを添加した四元
合金であり、かつカサ比重3.8gcm-3以上となる
ように形成した噴霧亜鉛合金粉末を負極活物質と
して用いることにより、水銀含有率2重量量%以
下の低汞化率ないし無汞化で使用した場合にアル
カリ電解液中における水素ガス発生が著しく少な
く、従つて貯蔵特性がよく環境的にも好ましいア
ルカリ電池を提供することができる。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
て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。 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
剤からなる薄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。 また本発明の技術は過酸化銀電池、酸化銀電
池、ニツケル・亜鉛電池、アルカリ・マンガン電
池、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。
[Table] In Table 1, D and E are examples of the present invention, A is a conventional example, and B and C are comparative examples. 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, and then 100μ
This is an atomized zinc powder with a viscosity ratio of 6.5% by weight, which is obtained by classifying the zinc powder into particles in the range of 300 μm to 300 μm and atomizing it with metallic mercury in a dilute NaOH solution. The bulk specific gravity of this product is slightly large at 3.12 g cm -3 , but this is because the true specific gravity is increased due to the high mercury content. The specific gravity is usually around 2.5g·cm -3 to 2.8g·cm -3 . Next, B in Table 1 is a comparative product, in which a zinc alloy containing 0.20% by weight of lead, 0.18% by weight of gallium, and 0.06% by weight of tin is granulated by the atomization method in the air.
After classification, a rare product containing the required amount of mercuric chloride
This is a low-fragility atomized zinc alloy powder with a viscosity rate of 1.37% by weight, obtained by treatment in a CH 3 COOH solution and viscosity. C in Table 1 is also a comparative product with 0.15% lead by weight.
This is an atomized atomized zinc alloy powder obtained by atomizing a zinc alloy containing 0.13% by weight of gallium and 0.025% by weight indium in the atmosphere, and then classifying it into particles in the range of 100 μm to 300 μm. In Table 1, D and E each represent an example of the present invention, and D has the same composition as B above.
A Ga-Sn based quaternary alloy is granulated by an atomization method in a nitrogen atmosphere, then classified to have a particle size of 100 μm to 300 μm, and then treated in a dilute CH 3 COOH solution containing the required amount of mercuric chloride. Obtained conversion rate
It is a 1.34% by weight low-fragility zinc alloy powder. Also E
is an aqueous atomized zinc alloy powder in which a Zn-Pb-Ga-In quaternary alloy having the same composition as C is granulated by the atomization method in a nitrogen gas atmosphere and then classified to have a grain size in the range of 100 μm to 300 μm. It is. As can be seen from the hydrogen gas generation rates in Table 1 B and C, multiple metallic elements selected from the group of elements belonging to Group b, Group b, Group b, Group b, and Group b of the Periodic Table. Even when the atomized zinc alloy powder to which an effective combination of the following is added is used at a lower rate of oxidation or no oxidation than conventional products, hydrogen gas generation is greatly reduced. In other words, with atomized zinc powder made in the same way from electrolytic zinc with a purity of 4N, for example, in the case of non-grading, even at a test temperature of 45°C, the 60% in Table 1 C is
This is because the hydrogen gas generation rate is several tens of times higher than the value at ℃. However, it can be seen that the amount of hydrogen gas generated is still large compared to the conventional products with a high conversion rate shown in Table 1A. On the other hand, in the case of the zinc spray alloy powder of the present invention shown in Table 1 D and E, which has a large bulk specific gravity, even if it is used with a low viscosity rate of 1.34% by weight or with no viscosity, the It can be seen that the hydrogen gas generation rate is halved compared to B and C, and the hydrogen gas generation rate is close to that of conventional example A, which has a high hydrogenation rate. The reason why the atomized 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 approximately 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 a shape model of a particle with a large diameter, and b is a shape model of a particle with a small breadth. The atomized zinc alloy particles of the present invention shown in Fig. 1 have significantly fewer sharp parts in the particle shape than the conventional product shown in Fig. 2, and the particle ends are rounded as a whole. Almost no wrinkle-like pattern is observed on the surface. In addition, the smaller the particle size, the more spherical it is compared to the conventional product, 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 1.6 to 1.0 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 fluidity (flow rate) is also improved because it reduces the friction between particles and makes it difficult to form bridges. There is. Further, as shown in Table 1, the zinc oxide content of the atomized zinc alloy powder having a large bulk specific gravity is extremely small. 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 deteriorate the pulse discharge characteristics. In addition, zinc oxide is a reaction product of batteries, and excessive inclusion means a decrease in the amount of active material.
It is desirable that the content thereof be as small as possible. [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 point of view, in the conventional case, molten zinc or molten zinc alloy extruded from a nozzle rapidly forms single molecules on the surface of clean droplet-shaped metal particles immediately after being atomized by air blow. An oxide film with a thickness of 1 to 30 mm or more is produced. The formation of an oxide film changes the interfacial tension of the liquid metal particles, and the individual particle shapes cool and solidify below the melting point before they are sufficiently affected by agglomeration due to the interfacial tension. Particles with various irregular shapes are produced depending on the acceleration, direction, gravity, etc., and sharp edges 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 the liquid metal particles with an oxide film formed on the surface change shape every moment as they move until they cool and solidify. It is thought that it was produced by repeatedly exposing a surface and reoxidizing that part. On the other hand, in the case shown in the embodiment of the present invention, molten zinc or molten zinc alloy extruded from a nozzle is sprayed into an inert gas atmosphere with high-pressure nitrogen gas, and when granulated, a liquid alloy is formed. Because the particle surface undergoes little or no oxidation, it is more susceptible to agglomeration and spheroidization due to interfacial tension, and the finer particles are less affected by acceleration and gravity until they are cooled below their melting point and solidified. It is thought that it easily becomes spherical. For particles with a large radius, the shape of the particle as a whole is difficult to become spherical and tends to become irregular due to the influence of gravity, etc., but locally the edges of the particle become rounded and the sharp edges are reduced, so the shape index is small. becomes. 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 increases. It seems that it is getting bigger. In any case, such favorable changes in characteristics are
It was found that by correlating with changes in the bulk specific gravity, it is possible to perform collective management based on the bulk specific gravity. As described above, the present invention is a quaternary alloy in which tin or indium is added to a ternary alloy of zinc-lead-gallium, and the atomized zinc alloy powder formed to have a bulk specific gravity of 3.8 gcm -3 or more is used to activate the negative electrode. By using it as a substance, hydrogen gas generation in the alkaline electrolyte is extremely small when used at a low or non-grading rate with a mercury content of 2% by weight or less, and therefore it has good storage characteristics and is environmentally friendly. A preferred alkaline battery can be provided. In addition, by using powder with a large bulk density in this way, the amount of active material in the same negative electrode volume can be increased,
In addition to improving rapid discharge characteristics at low temperatures, it is also possible to obtain gelled zinc negative electrodes that are easy to handle and have little variation in battery filling weight during volumetric measurement in the battery manufacturing process. It's big. 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. It can be applied to any of the so-called Powder With Gel methods in which a thin layer is formed and then gelled by injecting an alkaline electrolyte into the negative electrode container. The technology of the present invention also applies to various structures (cylindrical, button-shaped, coin-shaped, super It is effective when applied to alkaline batteries (flat type, etc.).

【図面の簡単な説明】[Brief explanation of drawings]

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。各図ともa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。
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. In each figure, a indicates the particle shape of a large particle, and b indicates a particle shape of a small particle.

Claims (1)

【特許請求の範囲】 1 負極活物質として、水銀汞化率が2重量%以
下で、かつ粒径が100〜300μmの亜鉛合金粉末を
用いるアルカリ電池において、 該亜鉛合金粉末は亜鉛−鉛−ガリウムの三元合
金に錫もしくはインジウムを添加した四元亜鉛合
金であり、さらにカサ比重が3.8gcm-3以上であ
り、平均形状指数(長径/短径)が1.6〜1.0であ
り、かつ酸化亜鉛が0.15重量%以下であることを
特徴としたアルカリ・亜鉛電池。
[Claims] 1. In an alkaline battery using a zinc alloy powder with a mercury conversion rate of 2% by weight or less and a particle size of 100 to 300 μm as a negative electrode active material, the zinc alloy powder is a zinc-lead-gallium powder. It is a quaternary zinc alloy made by adding tin or indium to a ternary alloy of An alkaline zinc battery characterized by a content of 0.15% by weight or less.
JP59104675A 1984-05-25 1984-05-25 Alkaline zinc battery Granted JPS6110860A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59104675A JPS6110860A (en) 1984-05-25 1984-05-25 Alkaline zinc battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59104675A JPS6110860A (en) 1984-05-25 1984-05-25 Alkaline zinc battery

Publications (2)

Publication Number Publication Date
JPS6110860A JPS6110860A (en) 1986-01-18
JPH0348619B2 true JPH0348619B2 (en) 1991-07-25

Family

ID=14387044

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59104675A Granted JPS6110860A (en) 1984-05-25 1984-05-25 Alkaline zinc battery

Country Status (1)

Country Link
JP (1) JPS6110860A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60262352A (en) * 1984-06-07 1985-12-25 Toshiba Battery Co Ltd Alkaline zinc battery

Family Cites Families (4)

* Cited by examiner, † Cited by third party
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
JPS5971259A (en) * 1982-10-18 1984-04-21 Mitsui Mining & Smelting Co Ltd Alkaline storage battery and its manufacturing method

Also Published As

Publication number Publication date
JPS6110860A (en) 1986-01-18

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