JP2003187797A - Positive pole active material for battery - Google Patents

Positive pole active material for battery

Info

Publication number
JP2003187797A
JP2003187797A JP2001388900A JP2001388900A JP2003187797A JP 2003187797 A JP2003187797 A JP 2003187797A JP 2001388900 A JP2001388900 A JP 2001388900A JP 2001388900 A JP2001388900 A JP 2001388900A JP 2003187797 A JP2003187797 A JP 2003187797A
Authority
JP
Japan
Prior art keywords
active material
powder
electrode active
positive electrode
battery
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
Application number
JP2001388900A
Other languages
Japanese (ja)
Other versions
JP4182233B2 (en
Inventor
Koji Tagami
幸治 田上
Yoshiyuki Masachi
吉行 正地
Yoshikazu Omoto
義和 尾本
Masayuki Nishina
正行 仁科
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.)
Dowa Holdings Co Ltd
Original Assignee
Dowa Mining 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 Dowa Mining Co Ltd filed Critical Dowa Mining Co Ltd
Priority to JP2001388900A priority Critical patent/JP4182233B2/en
Publication of JP2003187797A publication Critical patent/JP2003187797A/en
Application granted granted Critical
Publication of JP4182233B2 publication Critical patent/JP4182233B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • Y02E60/12

Landscapes

  • Primary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To reform powder to powder with high fluidity and packing property without affecting a battery characteristic by a positive pole active material of Ag-Bi-(M)-O system (M is Mn, Ni or Co or the like). <P>SOLUTION: The positive pole active material for the battery is powder comprising a particle containing the crystal of a compound comprising Ag, Bi and O (oxygen) or the crystal of a compound comprising Ag, Bi and M (M represents a transition metal), wherein Bi is dispersed in the whole area of the particle, and the angle of rest of the powder is not larger than 50 degree. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は,アルカリ電池用の
正極活物質に関する。
TECHNICAL FIELD The present invention relates to a positive electrode active material for alkaline batteries.

【0002】[0002]

【従来の技術】従来より,時計,計測機器,カメラ等に
装着されるアルカリ電池(通称ボタン電池)として酸化
銀電池が普及している。酸化銀電池は,正極活物質とし
て酸化銀(Ag2O),負極活物質として亜鉛末,電解
液としてアルカリ溶液例えばKOHやNaOHの水溶液
を用いて構成されるものが一般である。銀は高価な材料
であるが,酸化銀は小型でも高容量が要求される場合の
不可欠な正極活物質とされており,このためにボタン電
池の殆んどは酸化銀電池で構成されていると言っても過
言ではない。なお,正極活物質は正極作用物質または陽
極作用物質と呼ばれることもあり,同様に負極活物質は
負極作用物質または陰極作用物質と呼ばれることもあ
る。
2. Description of the Related Art Conventionally, silver oxide batteries have been widely used as alkaline batteries (commonly called button batteries) mounted on watches, measuring instruments, cameras and the like. A silver oxide battery is generally constructed by using silver oxide (Ag 2 O) as a positive electrode active material, zinc powder as a negative electrode active material, and an alkaline solution such as an aqueous solution of KOH or NaOH as an electrolytic solution. Although silver is an expensive material, silver oxide is considered to be an indispensable positive electrode active material when high capacity is required even if it is small. For this reason, most button batteries are composed of silver oxide batteries. It is no exaggeration to say that. The positive electrode active material may be referred to as a positive electrode active material or a positive electrode active material, and similarly, the negative electrode active material may be referred to as a negative electrode active material or a negative electrode active material.

【0003】前記のように銀は高価な物質である。この
ため,本発明者らは,酸化銀からなる電池用正極活物質
のコスト低減策として,特願2001−285788号
および特願2001−274194号において,要する
ところ,Ag,BiおよびO(酸素)からなる化合物の
結晶,またはAg,Bi,M(MはNi,CoまたはM
nなどの遷移金属を表す)およびOからなる化合物の結
晶,を有し,且つ粒子内全域にBiが分散している粒子
からなる電池用正極活物質を提案した。この正極活物質
ではAg含有量が75重量%以下であっても,従来の酸
化銀の場合と同等もしくはそれ以上の放電容量を有する
ので経済的である。
As mentioned above, silver is an expensive substance. Therefore, the inventors of the present invention, as a cost reduction measure of the positive electrode active material for a battery made of silver oxide, in Japanese Patent Application No. 2001-285788 and Japanese Patent Application No. 2001-274194 require Ag, Bi and O (oxygen). Or a crystal of a compound consisting of Ag, Bi, M (M is Ni, Co or M
The present invention has proposed a positive electrode active material for a battery, which comprises particles having a compound of O and a transition metal such as n) and having Bi dispersed throughout the particle. Even if the Ag content is 75% by weight or less, this positive electrode active material is economical because it has a discharge capacity equal to or higher than that of the conventional silver oxide.

【0004】[0004]

【発明が解決しようとする課題】特願2001−285
788号および特願2001−274194号で提案し
た正極活物質はAg量が少なく低コストであるが,その
製造履歴から粒子径が小さな(0.1〜10μm)粉体
となりやすく,このため,粉体の取り扱い性にさらなる
改良が求められていた。
[Problems to be Solved by the Invention] Japanese Patent Application No. 2001-285
Although the positive electrode active material proposed in Japanese Patent Application No. 788 and Japanese Patent Application No. 2001-274194 has a small amount of Ag and is low in cost, it tends to be a powder having a small particle size (0.1 to 10 μm) due to its manufacturing history. There has been a demand for further improvement in the handleability of the body.

【0005】すなわち,正極活物質としての取り扱いや
電池を製造する場合において,当該粉体の秤量作業や装
填作業は不可避であるが,このような場合に,より粉塵
の発生が少なく,流動性が良く,充填性に優れるといっ
た粉体特性が要求されていた。
That is, when handling as a positive electrode active material or manufacturing a battery, it is inevitable to weigh and load the powder, but in such a case, less dust is generated and fluidity is low. Good powder characteristics such as good filling property were required.

【0006】したがって本発明は,先に提案したAg−
Bi−(M)−O系の電池用正極活物質の粉体特性をさ
らに改善すること,より具体的には,粉塵発生が少な
く,優れた流動性および充填性を備えた正極活物質に改
善することを目的としたものである。
Therefore, the present invention is based on the previously proposed Ag-
Further improving the powder characteristics of the Bi- (M) -O-based positive electrode active material for a battery, more specifically, improving the positive electrode active material having less dust generation and excellent fluidity and filling property. The purpose is to do.

【0007】[0007]

【課題を解決するための手段】前記の課題を解決するた
め,本発明者らは先に提案したAg−Bi−(M)−O
系化合物の微細粒子からなる粉体に対して各種の造粒法
を適用し,その粉体の組成や化学的性質には実質的な変
化を与えることなく粉体特性を改善することを試みた。
その結果,数多くの造粒法のうち,噴霧造粒法または破
砕造粒法を採用して平均粒径を10μmより大きく,好
ましくは50μmより大きくすると安息角が50度以下
となり,前記の課題が一挙に解決できることがわかっ
た。
In order to solve the above-mentioned problems, the present inventors have previously proposed Ag-Bi- (M) -O.
Various granulation methods were applied to powders composed of fine particles of a series of compounds, and attempts were made to improve the powder properties without substantially changing the composition or chemical properties of the powders. .
As a result, among many granulation methods, when the spray granulation method or the crush granulation method is adopted and the average particle size is larger than 10 μm, preferably larger than 50 μm, the angle of repose becomes 50 degrees or less, and the above-mentioned problems occur. It turned out that it could be solved all at once.

【0008】すなわち本発明によれば,粉塵発生が少な
く優れた流動性および充填性を備えた正極活物質とし
て,Ag,BiおよびO(酸素)からなる化合物の結
晶,またはAg,Bi,M(Mは遷移金属を表す)およ
びOからなる化合物の結晶を有し且つ粒子内全域にBi
が分散している粒子からなる粉体であって,安息角が5
0度未満の粉体からなる電池用正極活物質を提供する。
この粉体の平均粒子径は10μmより大きく好ましくは
50μmより大きく,5mm以下好ましくは1mm以下
であり,嵩密度が1.0超え〜6.3g/cm3で,タップ密
度が1.5超え〜6.3g/cm3である。
That is, according to the present invention, as a positive electrode active material which generates little dust and has excellent fluidity and filling properties, a crystal of a compound composed of Ag, Bi and O (oxygen), or Ag, Bi, M ( M represents a transition metal) and a compound crystal of O and has Bi
Is a powder consisting of particles in which the angle of repose is 5
Provided is a positive electrode active material for a battery, which is made of powder having a temperature of less than 0 degree.
This powder has an average particle size of more than 10 μm, preferably more than 50 μm, 5 mm or less, preferably 1 mm or less, a bulk density of more than 1.0 to 6.3 g / cm 3 , and a tap density of more than 1.5 It is 6.3 g / cm 3 .

【0009】ここで,安息角は,濾紙を載せるホッパー
部とその中心から垂直に下降するノズル部をもつ通常の
化学実験用の漏斗であって,ホッパー部口径60mm,
ノズル長65mm,ノズル部内径6mmの漏斗を,その
ノズル先端が水平台から75mmの高さとなる位置に固
定したうえ,漏斗のホッパー部に粉体を100g投入
し,その全てが水平台の上に落下したときの堆積粉(円
錐形となる)の水平からの安息角を測定した値として定
義する。
Here, the angle of repose is a funnel for ordinary chemical experiments having a hopper portion on which a filter paper is placed and a nozzle portion vertically descending from the center, and the hopper portion has a diameter of 60 mm.
Fix a funnel with a nozzle length of 65 mm and a nozzle inner diameter of 6 mm at a position where the tip of the nozzle is at a height of 75 mm from the horizontal stand, and add 100 g of powder to the hopper of the funnel, all of which is on the horizontal stand. The angle of repose of the deposited powder (which becomes a cone) when dropped from the horizontal is defined as the measured value.

【0010】さらに本発明によれば,Ag,Biおよび
O(酸素)からなる化合物の結晶,またはAg,Bi,
M(Mは遷移金属を表す)およびOからなる化合物の結
晶を有し且つ粒子内全域にBiが分散している粒子から
なる粉体であって,BET法で測定した比表面積が0.
1〜30m2/g の粉体からなる電池用正極活物質を提
供する。
Further according to the present invention, a crystal of a compound consisting of Ag, Bi and O (oxygen), or Ag, Bi,
A powder comprising particles of a compound comprising M (M represents a transition metal) and O and having Bi dispersed throughout the particle, and having a specific surface area measured by the BET method of 0.1.
Provided is a positive electrode active material for a battery, which comprises 1 to 30 m 2 / g of powder.

【0011】[0011]

【発明の実施の形態】本発明は,前記のように特願20
01−285788号および特願2001−27419
4号で提案したAg−Bi−(M)−O系化合物の粒子
からなる正極活物質粉体に対して,粉塵が発生し難く流
動性および充填性に優れるという性質を付与することを
内容とするものである。このため,特願2001−28
5788号および特願2001−274194号の各明
細書および図面に記載した粉体の組成・性質・製造法等
についての説明は,そのまま本発明が対象とする粉体の
説明として援用できる。
BEST MODE FOR CARRYING OUT THE INVENTION As described above, the present invention is directed to Japanese Patent Application No.
01-285788 and Japanese Patent Application No. 2001-27419.
It is intended to impart to the positive electrode active material powder composed of the particles of the Ag-Bi- (M) -O-based compound proposed in No. 4 the property that dust is unlikely to be generated and the fluidity and the filling property are excellent. To do. Therefore, Japanese Patent Application No. 2001-28
The description of the composition, properties, manufacturing method, etc. of the powder described in the respective specifications and drawings of Japanese Patent No. 5788 and Japanese Patent Application No. 2001-274194 can be directly incorporated as the description of the powder targeted by the present invention.

【0012】すなわち,本発明に用いられるアルカリ電
池用正極活物質用の粉体は,基本的にはAg,Bi,
(M)およびOの4元素からなる粒子であり,この粒子
内に化合物結晶を有しており且つ粒子内全域にBiが分
散しているという特徴がある。Mは遷移元素から選ばれ
る一つ以上の元素であり,電池特性である開回路電圧を
低く押さえる目的で添加され,例えばNi,Co,Mn
が挙げられる。Mは場合によっては添加されないことも
ある。
That is, the powder for the positive electrode active material for alkaline batteries used in the present invention is basically composed of Ag, Bi,
The particles are composed of the four elements (M) and O, and are characterized in that compound crystals are contained in the particles and Bi is dispersed throughout the particles. M is one or more elements selected from transition elements, and is added for the purpose of keeping the open circuit voltage, which is a battery characteristic, low. For example, Ni, Co, Mn.
Is mentioned. M may not be added depending on the case.

【0013】粒子内の化合物結晶は,Ag−Bi−
(M)−O系の化合物であり,好ましくはAg2Oまた
はAgOの化合物の結晶を粒子内に有せず,有するとし
ても,不純物程度にしか有しないという特徴がある。こ
の粒子粉末はAg/(Bi+M)のモル比が1以上7以
下,好ましくは2以上5以下で且つ酸素含有量が5重量
%以上の組成を有している。Ag含有量は80重量%以
下,好ましくは75重量%以下,さらに好ましくは70
重量%以下,場合によっては60重量%以下であること
もできる。好ましい組成範囲は,重量%において,A
g:45〜75%,Bi:10〜40%,M:0〜10
%,O(酸素):5〜15%,残部:不可避的不純物で
ある。粒子の平均粒径は0.1〜10μmの範囲にあ
る。
The compound crystals in the particles are Ag-Bi-
It is a (M) -O-based compound, and is preferably characterized in that it does not have crystals of Ag 2 O or AgO compounds in the particles, and even if it does, it only has impurities. This particle powder has a composition in which the molar ratio Ag / (Bi + M) is 1 or more and 7 or less, preferably 2 or more and 5 or less and the oxygen content is 5% by weight or more. Ag content is 80% by weight or less, preferably 75% by weight or less, more preferably 70% by weight or less.
It can be less than or equal to 60% by weight, in some cases less than or equal to 60% by weight. The preferred composition range is, in% by weight, A
g: 45 to 75%, Bi: 10 to 40%, M: 0 to 10
%, O (oxygen): 5 to 15%, the balance: inevitable impurities. The average particle size of the particles is in the range of 0.1 to 10 μm.

【0014】このような正極活物質は,次のような工程
によって製造することができる。 (1) 銀,ビスマス,遷移金属の各塩とアルカリを水中で
反応させて中和澱物を得る工程(中和工程と言う),
(2) 得られた中和澱物の懸濁液に酸化剤を添加して該澱
物を酸化する工程(酸化工程),(3) 酸化澱物の懸濁液
を固液分離して澱物を回収する工程(分離工程),(4)
回収した酸化澱物を水洗乾燥する工程,(5) 得られた乾
燥物を解砕して粉体にする工程。各工程について説明す
ると次のとおりである。
Such a positive electrode active material can be manufactured by the following steps. (1) A step of reacting each salt of silver, bismuth, and transition metal with an alkali in water to obtain a neutralized precipitate (referred to as a neutralization step),
(2) a step of adding an oxidizing agent to the obtained suspension of neutralized starch to oxidize the starch (oxidation step), (3) solid-liquid separation of the suspension of the oxidized starch, Process for collecting things (separation process), (4)
A step of washing and drying the recovered oxidized starch, (5) a step of crushing the obtained dried material into a powder. Each step will be described below.

【0015】〔中和工程〕銀,ビスマス,遷移金属の塩
として,代表的には硝酸銀,硝酸ビスマス,硝酸ニッケ
ルなどを使用することができる。アルカリとしては強ア
ルカリ(例えば水酸化カリウム,水酸化ナトリウムのほ
か,水酸化リチウムなど)を使用する。中和処理は,ア
ルカリ水溶液に,銀,ビスマス,遷移金属の塩の水溶液
を添加する方法が適用できる。アルカリ度は高い方が反
応が進み易い。反応温度は室温から110℃までの範囲
が望ましく,中和反応が均一に進行する程度の攪拌が望
ましい。
[Neutralization Step] As a salt of silver, bismuth or a transition metal, silver nitrate, bismuth nitrate, nickel nitrate or the like can be typically used. A strong alkali (eg, potassium hydroxide, sodium hydroxide, lithium hydroxide, etc.) is used as the alkali. For the neutralization treatment, a method of adding an aqueous solution of a salt of silver, bismuth or a transition metal to an alkaline aqueous solution can be applied. The higher the alkalinity, the easier the reaction proceeds. The reaction temperature is preferably in the range of room temperature to 110 ° C., and stirring is preferably such that the neutralization reaction proceeds uniformly.

【0016】〔酸化工程〕中和工程と同時に行うことが
できるが,中和工程と酸化工程を分離して行うのが好ま
しく,これらの工程の間に昇温工程を挿入するのが好ま
しい。酸化剤としては,通常の酸化剤(例えばKMnO
4, NaOCl, H22, K228, Na228
オゾン等)を使用することができる。酸化処理は液温を
50℃以上,好ましくは70℃以上として攪拌下で酸化
剤を添加するのがよい。液温があまり高くなると酸化剤
の分解が進むので液温は110℃以下とするのがよい。
添加する酸化剤の量は,銀,ビスマス,遷移金属の価数
を上げるに十分な量であればよく,この価数変化の当量
以上,好ましくは2倍当量程度がよい。
[Oxidation Step] Although the neutralization step can be performed simultaneously, it is preferable to perform the neutralization step and the oxidation step separately, and it is preferable to insert a temperature raising step between these steps. As the oxidant, an ordinary oxidant (eg KMnO) is used.
4 , NaOCl, H 2 O 2 , K 2 S 2 O 8, Na 2 S 2 O 8 ,
Ozone etc.) can be used. For the oxidation treatment, it is preferable that the temperature of the liquid is 50 ° C. or higher, preferably 70 ° C. or higher and the oxidizing agent is added under stirring. If the liquid temperature becomes too high, the decomposition of the oxidant proceeds, so the liquid temperature is preferably 110 ° C. or lower.
The amount of the oxidizing agent added may be an amount sufficient to increase the valences of silver, bismuth, and a transition metal, and is equivalent to or more than this change in valence, preferably about twice the equivalent.

【0017】〔分離工程以降〕次いで,酸化澱物の固液
分離を処理を行うのであるが,その前に,酸化澱物を熟
成する工程を挿入するのが好ましい。この熟成工程は,
酸化処理後の懸濁液をその温度で10〜120分程度保
持する処理であり,これによって,酸化澱物の均一化を
図ることができる。澱物をろ別した後は,水洗し乾燥し
て黒色の澱物を得る。乾燥は50〜200℃の温度で行
うのがよい。200℃を超える温度では生成した化合物
が分解するおそれがある。得られた乾燥物は,粉砕機で
解砕することによって粉体を得る。
[After Separation Step] Next, solid-liquid separation of the oxidized starch is performed. Before that, it is preferable to insert a step of aging the oxidized starch. This aging process
This is a treatment in which the suspension after the oxidation treatment is held at that temperature for about 10 to 120 minutes, and thereby it is possible to make the oxidized starch uniform. After filtering off the starch, it is washed with water and dried to obtain a black starch. The drying is preferably performed at a temperature of 50 to 200 ° C. If the temperature exceeds 200 ° C, the produced compound may decompose. The obtained dried product is crushed with a crusher to obtain a powder.

【0018】このようにして得られる粉体は,前述のご
とく一般に平均粒子径が0.1〜10μmと小さく,流
動性や充填性が必ずしも良好ではない。これを改善する
ために,本発明においては,この粉体に対して噴霧造粒
もしくは破砕造粒による処理を行う。
The powder thus obtained generally has a small average particle size of 0.1 to 10 μm as described above, and does not necessarily have good flowability and filling property. In order to improve this, in the present invention, this powder is treated by spray granulation or crush granulation.

【0019】噴霧造粒は,水などの液媒体中に粉体を分
散させたスラリーを高温気流中に噴霧し,そのスラリー
滴が熱風と接触することによって,スラリー滴中の液が
瞬時に蒸発すると共に粒子同士が凝集して造粒されるも
のであり,噴霧ノズルの形状により, ディスク方式とノ
ズル方式が知られている。本発明が対象とするようなA
g−Bi−(M)−O系化合物からなる粉体に対して,
ディスク方式による噴霧造粒を適用するのがよいことが
わかった。
In spray granulation, a slurry in which a powder is dispersed in a liquid medium such as water is sprayed in a high temperature air stream, and the slurry droplets come into contact with hot air, whereby the liquid in the slurry droplets is instantly evaporated. At the same time, the particles agglomerate and are granulated, and the disk method and nozzle method are known depending on the shape of the spray nozzle. A as the subject of the present invention
For powders composed of g-Bi- (M) -O compounds,
It has been found to be good to apply spray granulation by the disc method.

【0020】破砕造粒は,粉末原料を高圧で圧縮成形す
ることによって密度の高い圧粉成形耐を得て,その成形
物を機械的に破砕および解砕し,ついで整粒して所定の
大きさの造粒物を得る方法である。本発明が対象とする
ようなAg−Bi−(M)−O系化合物からなる粉体は
高圧で圧縮成形すると密な成形品になり易い性質があ
り,これを適切に粉砕・解砕して整粒すれば,原料粉体
とは寸法および性状の異なる粉体が得られることがわか
った。
In the crushing and granulating method, a powder raw material is compression-molded at a high pressure to obtain a high-density powder compacting resistance, and the molded product is mechanically crushed and crushed, and then sized to a predetermined size. This is a method for obtaining granules of Sasa. The powder of Ag-Bi- (M) -O compound, which is the object of the present invention, tends to be a dense molded product when compression-molded at high pressure. It was found that if the particles were sized, a powder with different dimensions and properties from the raw powder could be obtained.

【0021】したがって,噴霧造粒もしくは破砕造粒に
よる粉体の二次処理を行うことによって,もとの粉体が
有する組成および化合物結晶の形態をそのまま維持し且
つ粒子内全域にBiが分散している造粒された粒子から
なる粉体が得られる。このようにして造粒された粒子か
らなる粉体は,平均粒子径が好ましくは10μmを超え
5mm以下であり,安息角が50度未満である。安息角
が低くなるほど粉体の流動性が良好となるが,本発明に
従うAg−Bi−(M)−O系の正極活物質は安息角が
50度未満,さらには45度以下,場合によっては40
度以下であり,電池製造にとって不可欠の精密秤量およ
びセルへの充填を作業性良く行うことができる。
Therefore, by subjecting the powder to secondary treatment by spray granulation or crush granulation, the composition and morphology of the compound crystals of the original powder are maintained as they are and Bi is dispersed throughout the particle. A powder consisting of the granulated particles is obtained. The average particle size of the powder formed from the particles thus granulated is preferably more than 10 μm and 5 mm or less, and the angle of repose is less than 50 degrees. The lower the angle of repose, the better the fluidity of the powder. However, the Ag-Bi- (M) -O-based positive electrode active material according to the present invention has a repose angle of less than 50 degrees, and even 45 degrees or less, depending on the case. 40
Since it is less than 100 degrees, it is possible to perform precise weighing and cell filling, which are indispensable for battery manufacturing, with good workability.

【0022】さらに,この造粒された粉体の嵩密度は
1.0超え〜6.3g/cm3,タップ密度は1.5超え〜6.
3g/cm3とすることができ,セルへの高充填に寄与でき
ることのほか,比表面積をBET法で30m2/g 以下
にできる。このことは微粉の含有量が非常に少ないこと
意味しており,このため粉塵の発生が少なくなる。
Further, the bulk density of the granulated powder exceeds 1.0 to 6.3 g / cm 3 , and the tap density exceeds 1.5 to 6.
It can be set to 3 g / cm 3 , which contributes to high filling of the cell and the specific surface area can be set to 30 m 2 / g or less by the BET method. This means that the content of fine powder is very low, which reduces the generation of dust.

【0023】したがって,本発明によると作業性が良く
且つ充填性の良いAg−Bi−(M)−O系化合物から
なる正極活物質が得られ,この正極活物質と,負極活物
質および電解質とによって安価で高性能なアルカリ電池
を構成することができる。
Therefore, according to the present invention, a positive electrode active material composed of an Ag-Bi- (M) -O type compound having good workability and good filling property can be obtained, and the positive electrode active material, the negative electrode active material and the electrolyte can be obtained. Thus, an inexpensive and high-performance alkaline battery can be constructed.

【0024】[0024]

【実施例】〔実施例1〕前述した中和工程において,A
g/(Bi+Ni)のモル比=3,Bi/Niのモル比
=1となるように硝酸銀 (AgNO3),硝酸ビスマス[Bi(NO
3)3]および硝酸ニッケル[ Ni(NO3)2・6 H2O ] を秤量し
て溶解した水溶液を,液温が50℃で(Ag+Bi+N
i)に対してモル比で10倍量の水酸化ナトリウムを溶
解した水溶液に,攪拌下で加え,中和澱物を得た。この
中和澱物の懸濁液を90℃に昇温し,酸化剤としてペル
オクソ2硫酸ナトリウム(Na2S2O8)を,(Ag+, Bi
3+,Ni2+)の価数変化の2倍量で,該懸濁液に添加し
て酸化処理した。酸化処理終了後,90℃の温度に30
分間保持する熟成を行ったあと,澱物を濾別し,水洗し
100℃で乾燥し,その乾燥品を解砕機で解粉して粉体
を得た。この粉体を〔中間粉〕と呼ぶ。
[Example] [Example 1] In the neutralization step described above, A
g / (Bi + Ni) molar ratio = 3, Bi / Ni molar ratio = 1, so that silver nitrate (AgNO 3 ) and bismuth nitrate [Bi (NO
3 ) 3 ] and nickel nitrate [Ni (NO 3 ) 2 .6 H 2 O] were weighed and dissolved to obtain an aqueous solution at a temperature of 50 ° C. (Ag + Bi + N
The mixture was added to an aqueous solution in which a molar ratio of sodium hydroxide was 10 times that of i) was dissolved under stirring to obtain a neutralized precipitate. The temperature of the suspension of the neutralized precipitate was raised to 90 ° C., and sodium peroxodisulfate (Na 2 S 2 O 8 ) was added as an oxidant (Ag + , Bi
3+ , Ni 2+ ) was added to the suspension in an amount twice as much as the change in valence, and the suspension was oxidized. After the oxidation process is completed, the temperature is raised to 90 ° C for 30
After aging for holding for 1 minute, the precipitate was filtered off, washed with water and dried at 100 ° C, and the dried product was pulverized with a crusher to obtain a powder. This powder is called [intermediate powder].

【0025】得られた中間粉から測定用試料をサンプリ
ングし,その嵩密度,タップ密度,安息角,粒度および
比表面積を測定し,その結果を表1に示した。またこの
中間粉の流動性,粉塵発生の程度,詰め込み性を評価
し,その結果も表1に示した。これらの測定は,次のよ
うにして行ったものである。
A sample for measurement was sampled from the obtained intermediate powder, and its bulk density, tap density, angle of repose, particle size and specific surface area were measured, and the results are shown in Table 1. The fluidity of the intermediate powder, the degree of dust generation, and the packing property were evaluated, and the results are also shown in Table 1. These measurements were performed as follows.

【0026】嵩密度の測定:直径15mm,高さ160
mmの試験管に粉末を充填し,その充填重量と充填体積
の測定値から求めた。 タップ密度の測定:嵩密度の測定と同じ試験管に粉末を
充填し,その充填重量と,充填させた粉末を1000回
タッピングしたあとの充填体積の測定値から求めた。 安息角の測定:化学実験用の漏斗であって,口径60m
m,ノズル長65mm,ノズル部内径6mmの漏斗を,
そのノズル先端が水平台から75mmの高さとなる位置
に固定し,漏斗のホッパー部に粉体を100g投入し,
その全てが水平台の上に円錐形となって堆積したときの
堆積物の水平からの角度を測定した。 粒度の測定:レーザー回折法(島津株式会社製の粒度測
定装置)によった。比表面積の測定:BET法(カンタ
クロム社製)によった。
Measurement of bulk density: diameter 15 mm, height 160
A mm test tube was filled with the powder, and it was determined from the measured values of the filling weight and the filling volume. Measurement of tap density: Powder was filled in the same test tube used for the measurement of bulk density, and the filling weight and the filling volume after tapping the filled powder 1000 times were determined. Measurement of angle of repose: Funnel for chemistry experiment, caliber 60m
m, nozzle length 65 mm, nozzle part inner diameter 6 mm,
The tip of the nozzle was fixed at a height of 75 mm from the horizontal table, and 100 g of powder was put into the hopper of the funnel.
The angle from the horizontal of the deposit was measured when all of them were deposited in a conical shape on the horizontal table. Measurement of particle size: by a laser diffraction method (particle size measuring device manufactured by Shimadzu Corporation). Measurement of specific surface area: BET method (manufactured by Kantachrome Co., Ltd.) was used.

【0027】流動性の評価:安息角が40度以下のもの
を流動性が良(○印),40度を超え50度未満のもの
を可(△),50度以上のを不可(×印)として3段階
評価を行った。 粉塵発生の評価:100CCの透明なポリ容器に粉体2
5gを入れ,10回振とうさせ,10秒間静置したとき
に容器上部に浮遊する粒子を目視観察し,浮遊物が認め
られないものを良(○印),浮遊物で曇った状態となっ
たものを不良(×印)とし,僅かに浮遊するものが認め
られるが,気にならない程度のものを可(△印)として
3段階評価を行った。 詰め込み性の評価:嵩密度が 2.0g/cm3以上のものを詰
め込み性が良(○印),1.0g/cm3を超え〜2.0 g/cm3
未満のものを詰め込み性が可(△印),1.0 g/cm3以下
のものを詰め込み性が不良(×印)として3段階評価を
行った。
Evaluation of fluidity: Fluidity is good when the angle of repose is 40 degrees or less (marked by ◯), acceptable when the angle of repose is more than 40 degrees and less than 50 degrees (△), and is not acceptable when it is greater than 50 degrees (marked x) ) Was evaluated in three stages. Evaluation of dust generation: Powder 2 in 100CC transparent plastic container
Put 5 g, shake 10 times, and visually observe the particles floating in the upper part of the container when left standing for 10 seconds. If no floating material is observed, it is good (marked with ○), and it becomes cloudy with floating material Those that were found to be defective (marked with x) and those that were slightly floating were recognized, but those that were not noticeable were evaluated as acceptable (marked with), and three-level evaluation was performed. Evaluation of packing property: Good packing property of bulk density of 2.0 g / cm 3 or more (circle), exceeding 1.0 g / cm 3 to 2.0 g / cm 3
Less than 1 is acceptable for packing (marked with Δ), and those with 1.0 g / cm 3 or less are considered for poor packing (marked with x), and three-level evaluation was performed.

【0028】表1の結果に見られるように,中間粉の流
動性および粉塵発生の評価は必ずしも良好ではなかっ
た。
As can be seen from the results in Table 1, the evaluation of the fluidity of the intermediate powder and the generation of dust was not always good.

【0029】次いで,中間粉を,大川原化工機株式会社
製のスプレードライヤーFOC−16を用いて熱風温度2
00℃で噴霧造粒を行った。得られた造粒品を〔造粒
粉〕と呼ぶ。造粒粉の電子顕微鏡(SEM像)観察では
65μm程度の球状粒子からなるものが殆んどであっ
た。造粒粉から測定用試料をサンプリングし,その嵩密
度,タップ密度,安息角,粒度および比表面積を測定
し,また造粒粉の流動性,粉塵発生の程度,詰め込み性
の評価した。それらの結果を表1に併記した。
Next, the intermediate powder was heated to a hot air temperature of 2 using a spray dryer FOC-16 manufactured by Okawara Kakoki Co., Ltd.
Spray granulation was performed at 00 ° C. The obtained granulated product is called [granulated powder]. Observation of the granulated powder by an electron microscope (SEM image) showed that most of them consisted of spherical particles of about 65 μm. A sample for measurement was sampled from the granulated powder, and its bulk density, tap density, angle of repose, particle size and specific surface area were measured, and the fluidity of the granulated powder, the degree of dust generation, and the packing property were evaluated. The results are also shown in Table 1.

【0030】表1の結果に見られるように,造粒粉の嵩
密度が高く且つ安息角が低くなって流動性が良好とな
り,粉塵発生も皆無となった。
As can be seen from the results shown in Table 1, the granulated powder has a high bulk density and a low angle of repose and has a good fluidity, and no dust is generated.

【0031】〔実施例2〕中間粉を得るまでは実施例1
を繰り返した。得られた中間粉を,ターボ工業株式会社
製WP160のローラーコンパクターを用いて圧粉成形
し,この成形物を日本グラニュレーター株式会社製GR
N−1531を用いて破砕し,造粒粉を得た。ここで,ロー
ラーコンパクターの成形圧力は 1.0 t/cm とした。ま
た,グラニュレーターによる破砕は三段階で行い,ロー
ルの一段目の溝ピッチは2mm(ロールクリアランス
0.35 mm), ロールの二段目の溝ピッチは 1.2mm
(ロールクリアランス 0.11 mm), ロールの三段目の
溝ピッチは 0.6mm(ロールクリアランス 0.11 mm)
とした。
Example 2 Example 1 was carried out until an intermediate powder was obtained.
Was repeated. The obtained intermediate powder was compacted by using a roller compactor of WP160 manufactured by Turbo Industry Co., Ltd., and this molded product was manufactured by Nippon Granulator Co., Ltd. GR.
The granulated powder was obtained by crushing with N-1531. Here, the molding pressure of the roller compactor was set to 1.0 t / cm. The crushing with a granulator is performed in three stages, and the groove pitch of the first stage of the roll is 2 mm (roll clearance
0.35 mm), the groove pitch of the second stage of the roll is 1.2 mm
(Roll clearance 0.11 mm), The groove pitch of the third roll is 0.6 mm (Roll clearance 0.11 mm)
And

【0032】この造粒粉から測定用試料をサンプリング
し,嵩密度,タップ密度,安息角,粒度および比表面積
を測定し,また造粒粉の流動性,粉塵発生の程度,詰め
込み性の評価した。それらの結果を表1に併記した。
A sample for measurement was sampled from this granulated powder, the bulk density, tap density, angle of repose, particle size and specific surface area were measured, and the fluidity of the granulated powder, the degree of dust generation, and the packing property were evaluated. . The results are also shown in Table 1.

【0033】さらに,造粒粉を目開き50μmの篩を用
いて50μm以下の粒子を除いた。得られた篩上の粉体
(整粒粉1と言う)から測定用試料をサンプリングし,
その嵩密度,タップ密度,安息角,粒度および比表面積
を測定し,また整粒粉の流動性,粉塵発生の程度,詰め
込み性の評価した。それらの結果を表1に併記した。
Further, the granulated powder was removed from particles having a size of 50 μm or less by using a sieve having an opening of 50 μm. A sample for measurement is sampled from the obtained powder on the sieve (referred to as sized powder 1),
The bulk density, tap density, angle of repose, particle size and specific surface area were measured, and the fluidity of the sized powder, the degree of dust generation, and the packing property were evaluated. The results are also shown in Table 1.

【0034】表1の結果から明らかなように,本例で
も,実施例1と同様に,流動性,粉塵発生および詰め込
み性の評価の良好な正極活物質が得られた。
As is clear from the results shown in Table 1, also in this example, as in the case of Example 1, a positive electrode active material excellent in evaluation of fluidity, dust generation and packing property was obtained.

【0035】次いで,造粒粉を目開き100μmの篩を
用いて100μm以下の粒子を除いた。得られた篩上の
粉体(整粒粉2と言う)から測定用試料をサンプリング
し,その嵩密度,タップ密度,安息角,粒度および比表
面積を測定し,また整粒粉の流動性,粉塵発生の程度,
詰め込み性の評価した。それらの結果を表1に併記し
た。
Then, the granulated powder was removed from particles having a size of 100 μm or less by using a sieve having a mesh size of 100 μm. A sample for measurement is sampled from the obtained powder on the sieve (referred to as sized powder 2), and its bulk density, tap density, angle of repose, particle size and specific surface area are measured, and the fluidity of the sized powder, Degree of dust generation,
The packing property was evaluated. The results are also shown in Table 1.

【0036】表1の結果に見られるように,整粒粉は嵩
密度およびタップ密度がさらに高くなり,比表面積が低
くなって,流動性,粉塵発生および詰め込み性の評価も
良好なものが得られた。
As can be seen from the results shown in Table 1, the sized powder has a higher bulk density and tap density, a lower specific surface area, and has a good evaluation of fluidity, dust generation and packing property. Was given.

【0037】〔比較例〕前述した中和工程において,A
g/(Bi+Ni)のモル比=3,Bi/Niのモル比
=0.5となるように硝酸銀 (AgNO3),硝酸ビスマス[Bi
(NO3)3]および硝酸ニッケル[ Ni(NO3)2・6 H2O ] を秤
量して溶解した水溶液を,液温が50℃で(Ag+Bi
+Ni)に対してモル比で10倍量の水酸化ナトリウム
を溶解した水溶液に,攪拌下で加え,中和澱物を得た。
この中和澱物の懸濁液を90℃に昇温し,酸化剤として
ペルオクソ2硫酸ナトリウム(Na2S2O8)を,(Ag+,
Bi3+, Ni2+)の価数変化の2倍量で,該懸濁液に添
加して酸化処理した。酸化処理終了後,90℃の温度に
30分間保持する熟成を行ったあと,澱物を濾別し,水
洗し100℃で乾燥し,その乾燥品を解砕機で解粉して
粉体を得た。
[Comparative Example] In the neutralization step described above, A
g / (Bi + Ni) molar ratio = 3, Bi / Ni molar ratio = 0.5 so that silver nitrate (AgNO 3 ) and bismuth nitrate [Bi
An aqueous solution in which (NO 3 ) 3 ] and nickel nitrate [Ni (NO 3 ) 2 .6 H 2 O] were weighed and dissolved at a liquid temperature of 50 ° C (Ag + Bi
+ Ni) was added to an aqueous solution in which a molar ratio of 10 times the amount of sodium hydroxide was dissolved under stirring to obtain a neutralized precipitate.
The temperature of the suspension of the neutralized precipitate was raised to 90 ° C., and sodium peroxodisulfate (Na 2 S 2 O 8 ) was added as an oxidant (Ag + ,
Bi 3+ , Ni 2+ ) was added to the suspension in an amount twice as much as the change in valence, and an oxidation treatment was performed. After completion of the oxidation treatment, aging was carried out by keeping the temperature at 90 ° C for 30 minutes, then the precipitate was filtered off, washed with water and dried at 100 ° C, and the dried product was pulverized with a crusher to obtain a powder. It was

【0038】この粉体から測定用試料をサンプリング
し,その嵩密度,タップ密度,安息角,粒度および比表
面積を測定し,その結果を表1に示した。また粉体の流
動性,粉塵発生の程度,詰め込み性を評価し,その結果
も表1に示した。
A sample for measurement was sampled from this powder, and the bulk density, tap density, angle of repose, particle size and specific surface area were measured, and the results are shown in Table 1. The fluidity of the powder, the degree of dust generation, and the packing property were evaluated, and the results are also shown in Table 1.

【0039】[0039]

【表1】 [Table 1]

【0040】表1に見られるように,特願2001−2
85788号や特願2001−274194号で提案し
たAg−Bi−(M)−O系の正極活物質は,噴霧造粒
または破砕造粒によって取り扱い易い粉体に改変するこ
とができる。この正極活物質は高価なAgを含む関係
上,電池製品に組み込まれるまでに歩留り良く取り扱わ
れることが求められが,噴霧造粒または破砕造粒によっ
てこの要求が十分に満たされたことがわかる。
As shown in Table 1, Japanese Patent Application No. 2001-2
The Ag-Bi- (M) -O-based positive electrode active material proposed in Japanese Patent Application No. 85788 and Japanese Patent Application No. 2001-274194 can be converted into a powder that is easy to handle by spray granulation or crush granulation. Since this positive electrode active material contains expensive Ag, it is required to be handled with a good yield before being incorporated into a battery product, and it can be seen that this requirement was sufficiently satisfied by spray granulation or crush granulation.

【0041】[0041]

【発明の効果】以上説明したように,本発明によれば,
Ag量を低減しても酸化銀と同等の電池特性を有するA
g−Bi−(M)−O系の正極活物質に対して,その電
池特性には影響を与えないで,取り扱い易い粉体に改善
することができるので,電池製造までの作業性の向上と
歩留りの向上に寄与することができる。
As described above, according to the present invention,
A that has the same battery characteristics as silver oxide even if the amount of Ag is reduced
With respect to the g-Bi- (M) -O-based positive electrode active material, it is possible to improve the powder to an easy-to-handle powder without affecting the battery characteristics. It can contribute to the improvement of the yield.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 尾本 義和 東京都千代田区丸の内1丁目8番2号 同 和鉱業株式会社内 (72)発明者 仁科 正行 東京都千代田区丸の内1丁目8番2号 同 和鉱業株式会社内 Fターム(参考) 5H024 AA01 AA04 CC03 HH00 HH01 HH08 HH13 5H050 AA19 BA04 CA07 CB13 FA17 FA19 HA00 HA02 HA05 HA07 HA08    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Yoshikazu Omoto             1-8-2 Marunouchi, Chiyoda-ku, Tokyo             Within Wa Mining Co., Ltd. (72) Inventor Masayuki Nishina             1-8-2 Marunouchi, Chiyoda-ku, Tokyo             Within Wa Mining Co., Ltd. F-term (reference) 5H024 AA01 AA04 CC03 HH00 HH01                       HH08 HH13                 5H050 AA19 BA04 CA07 CB13 FA17                       FA19 HA00 HA02 HA05 HA07                       HA08

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 Ag,BiおよびO(酸素)からなる化
合物の結晶,またはAg,Bi,M(Mは遷移金属を表
す)およびOからなる化合物の結晶を有し且つ粒子内全
域にBiが分散している粒子からなる粉体であって,安
息角が50度未満の粉体からなる電池用正極活物質。
1. A crystal of a compound consisting of Ag, Bi and O (oxygen), or a crystal of a compound consisting of Ag, Bi, M (M represents a transition metal) and O, and Bi is distributed throughout the particle. A positive electrode active material for a battery, which is a powder composed of dispersed particles and has a repose angle of less than 50 degrees.
【請求項2】 平均粒子径が10μmを超え5mm以下
である請求項1に記載の電池用正極活物質。
2. The positive electrode active material for a battery according to claim 1, which has an average particle size of more than 10 μm and 5 mm or less.
【請求項3】 嵩密度が1.0超え〜6.3g/cm3でタッ
プ密度が1.5超え〜6.3g/cm3である請求項1または
2に記載の電池用正極活物質。
3. The positive electrode active material for a battery according to claim 1, which has a bulk density of more than 1.0 to 6.3 g / cm 3 and a tap density of more than 1.5 to 6.3 g / cm 3 .
【請求項4】 Ag,BiおよびO(酸素)からなる化
合物の結晶,またはAg,Bi,M(Mは遷移金属を表
す)およびOからなる化合物の結晶を有し且つ粒子内全
域にBiが分散している粒子からなる粉体であって,B
ET法で測定した比表面積が0.1〜30m2/g の粉体
からなる電池用正極活物質。
4. A crystal of a compound consisting of Ag, Bi and O (oxygen), or a crystal of a compound consisting of Ag, Bi, M (M represents a transition metal) and O, and Bi is distributed throughout the particle. A powder consisting of dispersed particles, B
A positive electrode active material for a battery, which comprises a powder having a specific surface area of 0.1 to 30 m 2 / g measured by the ET method.
【請求項5】 Ag2OまたはAgOの結晶を粒子内に
有しないかまたは不純物程度にしか有しない請求項1な
いし4のいずれかに記載の電池用正極活物質。
5. The positive electrode active material for a battery according to claim 1, which does not have Ag 2 O or AgO crystals in the particles or has only an impurity level.
【請求項6】 粒子は,Ag/(Bi+M)のモル比が
1以上7以下で且つ酸素含有量が5重量%以上の組成を
有する請求項1ないし5のいずれかに記載の電池用正極
活物質。
6. The positive electrode active material for a battery according to claim 1, wherein the particles have a composition in which the molar ratio Ag / (Bi + M) is 1 or more and 7 or less and the oxygen content is 5% by weight or more. material.
【請求項7】 粒子中のAg含有量は75重量%以下で
ある請求項1ないし6のいずれかに記載の電池用正極活
物質。
7. The positive electrode active material for a battery according to claim 1, wherein the Ag content in the particles is 75% by weight or less.
【請求項8】 負極活物質,正極活物質および電解質か
らなるアルカリ電池において,正極活物質として請求項
1ないし7のいずれかに記載された正極活物質が用いら
れたアルカリ電池。
8. An alkaline battery comprising a negative electrode active material, a positive electrode active material and an electrolyte, wherein the positive electrode active material according to any one of claims 1 to 7 is used as the positive electrode active material.
JP2001388900A 2001-12-21 2001-12-21 Positive electrode active material for batteries Expired - Fee Related JP4182233B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005001964A1 (en) * 2003-06-30 2005-01-06 Zeon Corporation Compounding agent composition for cathode film, polyether polymer composition for cathode film
JP2005056714A (en) * 2003-08-05 2005-03-03 Matsushita Electric Ind Co Ltd Positive electrode mixture and alkaline dry cell using the same
JP2007506252A (en) * 2003-09-16 2007-03-15 ザ ジレット カンパニー Primary alkaline battery with bismuth metal oxide
JP2015026432A (en) * 2013-07-24 2015-02-05 日本ゼオン株式会社 Composite particle with reduced particle size for electrochemical element electrode and method for producing composite particle with reduced particle size for electrochemical element electrode

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005001964A1 (en) * 2003-06-30 2005-01-06 Zeon Corporation Compounding agent composition for cathode film, polyether polymer composition for cathode film
JP2005056714A (en) * 2003-08-05 2005-03-03 Matsushita Electric Ind Co Ltd Positive electrode mixture and alkaline dry cell using the same
JP2007506252A (en) * 2003-09-16 2007-03-15 ザ ジレット カンパニー Primary alkaline battery with bismuth metal oxide
JP2015026432A (en) * 2013-07-24 2015-02-05 日本ゼオン株式会社 Composite particle with reduced particle size for electrochemical element electrode and method for producing composite particle with reduced particle size for electrochemical element electrode

Also Published As

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