JP2002003223A - Surface electroconductive oxy nickel hydroxide and method for manufacturing it - Google Patents

Surface electroconductive oxy nickel hydroxide and method for manufacturing it

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Publication number
JP2002003223A
JP2002003223A JP2000181061A JP2000181061A JP2002003223A JP 2002003223 A JP2002003223 A JP 2002003223A JP 2000181061 A JP2000181061 A JP 2000181061A JP 2000181061 A JP2000181061 A JP 2000181061A JP 2002003223 A JP2002003223 A JP 2002003223A
Authority
JP
Japan
Prior art keywords
nickel oxyhydroxide
hydroxide
nickel hydroxide
cobalt
aqueous solution
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
JP2000181061A
Other languages
Japanese (ja)
Other versions
JP3505133B2 (en
Inventor
Takeshi Usui
臼井  猛
Junichi Imaizumi
純一 今泉
Tokuyoshi Iida
得代志 飯田
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.)
Tanaka Chemical Corp
Original Assignee
Tanaka Chemical Corp
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Publication date
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Priority to JP2000181061A priority Critical patent/JP3505133B2/en
Publication of JP2002003223A publication Critical patent/JP2002003223A/en
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Publication of JP3505133B2 publication Critical patent/JP3505133B2/en
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    • 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

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  • Inorganic Compounds Of Heavy Metals (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a surface electroconductive oxy nickel hydroxide and a method for manufacturing it. SOLUTION: The surface electoconductive oxy nickel hydroxide concerned to this invention has a characteristic that it is produced by two processes consisted with the first process in which particles of nickel oxide and cobalt salt are reacted in the solution of pH 5-11 to get intermediate product and the second process in which the aforesaid intermediate product is oxidized in the solution and it has superior electro conductivity.

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、表面導電性オキシ
水酸化ニッケルおよびその製造方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a surface conductive nickel oxyhydroxide and a method for producing the same.

【0002】[0002]

【従来の技術】表面導電性オキシ水酸化ニッケルは、水
溶液中で水酸化ニッケルを酸化してオキシ水酸化ニッケ
ルにする工程Aと、得られたオキシ水酸化ニッケルを水
溶液中でコバルト塩と反応させてコバルト化合物により
被覆されたオキシ水酸化ニッケルを得る工程Bと、これ
をさらに水酸化ナトリウム水溶液で長時間に渡り加熱処
理させる工程Cとからなる方法により製造されている
(特願平10−214622)。また、得られる表面導
電性オキシ水酸化ニッケルの表面導電性は必ずしも十分
ではなく、さらに表面導電性に優れる表面導電性オキシ
水酸化ニッケルの提供が望まれていた。
2. Description of the Related Art Surface-conductive nickel oxyhydroxide is obtained by oxidizing nickel hydroxide in an aqueous solution to form nickel oxyhydroxide, and reacting the obtained nickel oxyhydroxide with a cobalt salt in an aqueous solution. (Step B) of obtaining a nickel oxyhydroxide coated with a cobalt compound by heating and a step C of subjecting this to a long-time heat treatment with an aqueous sodium hydroxide solution (Japanese Patent Application No. 10-214622). ). In addition, the surface conductivity of the resulting surface-conductive nickel oxyhydroxide is not always sufficient, and it has been desired to provide a surface-conductive nickel oxyhydroxide having excellent surface conductivity.

【0003】[0003]

【課題を解決するための手段】本発明者は、pH5〜1
1の水溶液中で粒状水酸化ニッケルとコバルト塩とを反
応させて得られる中間体を、さらに水溶液中で酸化して
得られる表面導電性オキシ水酸化ニッケルが表面導電性
に優れることを見出し本発明を完成した。すなわち本発
明は、pH5〜11の水溶液中で粒状水酸化ニッケルと
コバルト塩とを反応させて中間体を得る工程1と、前記
得られた中間体を水溶液中で酸化する工程2とからなる
表面導電性オキシ水酸化ニッケル製造方法を提供するも
のである。
Means for Solving the Problems The inventor of the present invention has a pH of 5-1.
The present inventors have found that a surface conductive nickel oxyhydroxide obtained by further oxidizing an intermediate obtained by reacting granular nickel hydroxide and a cobalt salt in an aqueous solution in aqueous solution is excellent in surface conductivity. Was completed. That is, the present invention provides a surface comprising a step 1 of reacting granular nickel hydroxide and a cobalt salt in an aqueous solution having a pH of 5 to 11 to obtain an intermediate, and a step 2 of oxidizing the obtained intermediate in an aqueous solution. An object of the present invention is to provide a method for producing conductive nickel oxyhydroxide.

【0004】また、本発明は前記工程1において、前記
pHが9〜11の範囲であり、かつ前記水溶液中にアン
モニウム塩が溶解していることを特徴とする前記記載の
表面導電性オキシ水酸化ニッケル製造方法を提供するも
のである。さらに、本発明は表面導電性に優れた表面導
電性オキシ水酸化ニッケルを提供するものである。
Further, the present invention is characterized in that, in the step 1, the pH is in the range of 9 to 11, and an ammonium salt is dissolved in the aqueous solution. A method for producing nickel is provided. Further, the present invention provides a surface conductive nickel oxyhydroxide having excellent surface conductivity.

【0005】[0005]

【発明の実施の形態】製造方法 本発明に係る表面導電性オキシ水酸化ニッケル製造方法
は、pH5〜11の水溶液中で粒状水酸化ニッケルとコ
バルト塩とを反応させて中間体を得る工程1と、前記得
られた中間体を水溶液中で酸化する工程2とからなるこ
とを特徴とする。なお、得られる中間体および表面導電
性オキシ水酸化ニッケルの性質、形状等は、反応容器の
形状、攪拌方法、反応溶液中の反応物の濃度、反応時間
等に依存するが、これらの反応条件を適宜選択し最適化
することは当業者により容易である。
BEST MODE FOR CARRYING OUT THE INVENTION The production method of a surface-conductive nickel oxyhydroxide according to the present invention comprises a step 1 of reacting granular nickel hydroxide with a cobalt salt in an aqueous solution having a pH of 5 to 11 to obtain an intermediate. And oxidizing the obtained intermediate in an aqueous solution. The properties, shapes, etc. of the obtained intermediate and surface conductive nickel oxyhydroxide depend on the shape of the reaction vessel, the stirring method, the concentration of the reactants in the reaction solution, the reaction time, etc. It is easier for those skilled in the art to appropriately select and optimize

【0006】(工程1)前記工程1におけるpHの値は
5以上であればよい。pHの範囲はより好ましくはpH
5〜11である。反応溶液のpH値は、例えばアルカリ
金属水酸化物を適時添加して調整し、一定に保つことが
できる。アルカリ金属水酸化物は、好ましくは水酸化ナ
トリウム、水酸化カリウムである。さらに、前記工程1
における反応溶液中にはアンモニウム塩を添加すること
もできる。アンモニウム塩は、例えば硫酸アンモニウ
ム、塩化アンモニウムである。反応温度は、20〜60
℃の範囲が好ましい。より好ましくは、下限は30℃、
上限は50℃である。さらに好ましくは、下限は35
℃、上限は45℃である。
(Step 1) The pH value in step 1 may be 5 or more. The pH range is more preferably pH
5 to 11. The pH value of the reaction solution can be kept constant, for example, by adding an alkali metal hydroxide as needed. The alkali metal hydroxide is preferably sodium hydroxide or potassium hydroxide. Further, the step 1
An ammonium salt can also be added to the reaction solution in the above. The ammonium salt is, for example, ammonium sulfate or ammonium chloride. The reaction temperature is 20-60
C. is preferred. More preferably, the lower limit is 30 ° C,
The upper limit is 50 ° C. More preferably, the lower limit is 35
° C, the upper limit is 45 ° C.

【0007】工程1で使用する原料としての粒状水酸化
ニッケルは、平均粒径が6〜15μmのものが好まし
い。さらに水酸化ニッケルは他の金属が含まれる共晶体
も使用できる。他の金属としては、Zn、Coを挙げら
れる。水分量が0.6%の状態でZnを0.1〜6.0wt
%、Coを0.1〜5.0wt%含む共晶である水酸化ニッ
ケルを使用することができる。工程1で使用可能なコバ
ルト塩は、水溶液中で2価のコバルトイオンになるコバ
ルト塩であればよい。例えば硫酸コバルト、硝酸コバル
ト、塩化コバルトを挙げることができる。
The granular nickel hydroxide used as a raw material in the step 1 preferably has an average particle size of 6 to 15 μm. Further, eutectic containing other metals can also be used as nickel hydroxide. Other metals include Zn and Co. When the water content is 0.6%, Zn is added in an amount of 0.1 to 6.0 wt.
%, And eutectic nickel hydroxide containing 0.1 to 5.0 wt% of Co can be used. The cobalt salt that can be used in step 1 may be a cobalt salt that becomes divalent cobalt ion in an aqueous solution. For example, cobalt sulfate, cobalt nitrate, and cobalt chloride can be mentioned.

【0008】工程1で得られる中間体は、表面を水酸化
コバルトで被覆された水酸化ニッケルである。具体的に
は、水酸化コバルトはα型、β型またはこれらの混合物
であると考えられる。水酸化コバルトは、好ましくはα
型水酸化コバルトである。また必要により、前記得られ
た中間体は水洗して工程2の原料として使用することが
できる。さらに必要により、前記得られた中間体は分離
して工程2の原料として使用することもできる。例え
ば、分離方法として濾過を挙げられる。また必要によ
り、前記得られた中間体は乾燥して工程2の原料として
使用することもできる。例えば、乾燥方法として温風乾
燥、真空乾燥を挙げることができる。
The intermediate obtained in step 1 is nickel hydroxide whose surface is coated with cobalt hydroxide. Specifically, the cobalt hydroxide is considered to be α-form, β-form or a mixture thereof. The cobalt hydroxide is preferably α
Type cobalt hydroxide. If necessary, the obtained intermediate can be washed with water and used as a raw material in step 2. Further, if necessary, the obtained intermediate can be separated and used as a raw material in step 2. For example, filtration can be mentioned as a separation method. If necessary, the obtained intermediate can be dried and used as a raw material in step 2. For example, drying methods include hot air drying and vacuum drying.

【0009】(工程2)工程2では反応器に水と前記工
程1で得られる中間体を添加し攪拌する。さらに水に溶
かした酸化剤を添加して加熱し数時間反応させて表面導
電性オキシ水酸化ニッケルを得る。工程2において使用
可能な酸化剤は、工程1で得られる中間体の水酸化コバ
ルトおよび水酸化ニッケルを酸化するものであればよ
い。例えば、次亜塩素酸ナトリウム、次亜塩素酸カリウ
ム、過硫酸ナトリウム、過硫酸カリウムである。使用可
能な酸化剤は、好ましくは次亜塩素酸ナトリウム、次亜
塩素酸カリウムである。反応温度は、20〜70℃の範
囲が好ましい。より好ましくは、下限は30℃、上限は
60℃である。さらに好ましくは、下限は35℃、上限
は55℃である。また必要により、前記得られた表面導
電性オキシ水酸化ニッケルは水洗することができる。さ
らに必要により、前記得られた表面導電性オキシ水酸化
ニッケルは乾燥することもできる。例えば、乾燥方法と
して温風乾燥、真空乾燥を挙げることができる。
(Step 2) In step 2, water and the intermediate obtained in step 1 are added to a reactor and stirred. Further, an oxidizing agent dissolved in water is added, and the mixture is heated and reacted for several hours to obtain surface conductive nickel oxyhydroxide. The oxidizing agent that can be used in the step 2 may be any one that oxidizes the intermediate cobalt hydroxide and nickel hydroxide obtained in the step 1. For example, sodium hypochlorite, potassium hypochlorite, sodium persulfate, and potassium persulfate. Oxidizing agents that can be used are preferably sodium hypochlorite and potassium hypochlorite. The reaction temperature is preferably in the range of 20 to 70C. More preferably, the lower limit is 30 ° C and the upper limit is 60 ° C. More preferably, the lower limit is 35 ° C and the upper limit is 55 ° C. If necessary, the obtained surface conductive nickel oxyhydroxide can be washed with water. Further, if necessary, the obtained surface conductive nickel oxyhydroxide can be dried. For example, drying methods include hot air drying and vacuum drying.

【0010】表面導電性オキシ水酸化ニッケル 本発明の製造方法により得られる表面導電性オキシ水酸
化ニッケルは、表面がコバルト化合物で被覆されている
オキシ水酸化ニッケルであり、優れた表面導電性を有す
る。電子顕微鏡によりコバルト化合物で被覆されたオキ
シ水酸化ニッケルの表面を観察した結果、図1および図
2に示されたように、コバルト化合物でオキシ水酸化ニ
ッケルの表面が均一に被覆されていることを確認でき
る。
Surface-conductive nickel oxyhydroxide The surface-conductive nickel oxyhydroxide obtained by the production method of the present invention is nickel oxyhydroxide whose surface is coated with a cobalt compound and has excellent surface conductivity. . As a result of observing the surface of the nickel oxyhydroxide coated with the cobalt compound with an electron microscope, it was confirmed that the surface of the nickel oxyhydroxide was uniformly coated with the cobalt compound as shown in FIGS. 1 and 2. You can check.

【0011】[0011]

【実施例】実施例1 攪拌機を備えた15Lの円筒型反応槽に水を10L入れ
た後、温度を40℃に保持して一定速度にて攪拌を行っ
た。水酸化ニッケル(水分量が0.6%の乾燥粒状でZ
nを4.0wt%、Coを1.5wt%含む共晶、平均粒径が
10.5μmの球状)1.2kgを反応槽に加えた。加えた
水酸化ニッケルが均一に分散する攪拌速度を保った状態
で、硫酸コバルト水溶液(Coを84g/L含有)を1
0ml/分の速度で100分間連続的に反応槽へ添加し
た。反応中は、反応溶液のpHが常に8.0を保つよう
に断続的に30wt%水酸化ナトリウム水溶液を加えた。
反応槽内の粒状物を水洗、濾過し、60℃にて15時間
乾燥した。その結果、水酸化ニッケルの表面に水酸化コ
バルトが被覆した緑色の乾燥粒状中間体を得た。
Example 1 10 L of water was put into a 15 L cylindrical reaction vessel equipped with a stirrer, and the mixture was stirred at a constant speed while maintaining the temperature at 40 ° C. Nickel hydroxide (dry granules with water content of 0.6%, Z
1.2 kg of a eutectic containing 4.0 wt% of n and 1.5 wt% of Co and having a mean particle diameter of 10.5 μm) were added to the reaction vessel. While maintaining the stirring speed at which the added nickel hydroxide is uniformly dispersed, 1 part of an aqueous solution of cobalt sulfate (containing 84 g / L of Co) is added.
It was continuously added to the reactor at a rate of 0 ml / min for 100 minutes. During the reaction, a 30 wt% aqueous sodium hydroxide solution was added intermittently so that the pH of the reaction solution was always maintained at 8.0.
The granular material in the reaction tank was washed with water, filtered, and dried at 60 ° C. for 15 hours. As a result, a green dry granular intermediate in which the surface of nickel hydroxide was coated with cobalt hydroxide was obtained.

【0012】次に、攪拌機を備えた15Lの円筒型反応
槽に水を6L入れ、前記にて得られた中間体1.2kgを
加えて一定速度にて攪拌を行った。ここに次亜塩素酸ナ
トリウム水溶液(有効塩素量14%)4Lを加え、反応
温度を50℃に保持して2時間反応させた。反応終了
後、反応槽内の粒状物を水洗、濾過し、80℃にて15
時間乾燥した。その結果、コバルト化合物で被覆された
オキシ水酸化ニッケル(黒色粒状体)を得た。得られた
黒色粒状体に10N/cm2の圧力を掛けて厚さ2mmの板
状固形体を作成した。この固形体の厚さ方向で、抵抗値
を測定したところ0.93Ωであった。また、得られた
黒色粒状体の平均粒径(堀場製作所製LA−910を使
用し、操作手順書に従った。)は10.6μmであっ
た。また、黒色粒状体についてX線回折分析(黒色粒状
体をそのまま使用し、株式会社理学製、RINT200
0(Cu−Kα)を用い、操作手順書に従った。)を行
った結果、β型オキシ水酸化ニッケルが有するピークと
一致していた(JCPDSカード番号=60141)。
Next, 6 L of water was put into a 15 L cylindrical reaction vessel equipped with a stirrer, and 1.2 kg of the intermediate obtained above was added thereto, followed by stirring at a constant speed. 4 L of an aqueous solution of sodium hypochlorite (available chlorine amount: 14%) was added thereto, and the reaction was performed for 2 hours while maintaining the reaction temperature at 50 ° C. After completion of the reaction, the particulate matter in the reaction tank was washed with water, filtered,
Dried for hours. As a result, nickel oxyhydroxide (black granular material) coated with the cobalt compound was obtained. A pressure of 10 N / cm 2 was applied to the obtained black granular material to produce a plate-like solid having a thickness of 2 mm. When the resistance was measured in the thickness direction of the solid, it was 0.93Ω. The average particle size of the obtained black granular material (using LA-910 manufactured by HORIBA, Ltd. and following the operating procedure) was 10.6 μm. Further, X-ray diffraction analysis of the black granules (using the black granules as they are, RINT200 manufactured by Rigaku Corporation)
Using 0 (Cu-Kα), the operating procedure was followed. ) Was consistent with the peak of β-type nickel oxyhydroxide (JCPDS card number = 60141).

【0013】実施例2 攪拌機を備えた15Lの円筒型反応槽に水を10L入れ
た後、硫酸アンモニウム400gを加えて溶解させた。
ここに、pHが10.5となるように30wt%水酸化ナ
トリウム水溶液を加え、温度を40℃に保持して一定速
度にて攪拌を行った。これ以降の操作は、反応溶液のp
Hが常に10.5を保つようにした以外は実施例1と同
様の操作および測定を行った。その結果、導電性を有す
るコバルト化合物で被覆されたオキシ水酸化ニッケルの
黒色乾燥粒状体を得た。抵抗値は0.90Ωであり、平
均粒径は10.5μmであった。また、β型オキシ水酸
化ニッケルが有するピークとも一致していた(JCPD
Sカード番号=60141)。
Example 2 10 L of water was put into a 15 L cylindrical reaction tank equipped with a stirrer, and 400 g of ammonium sulfate was added to dissolve it.
Here, a 30 wt% aqueous sodium hydroxide solution was added so that the pH became 10.5, and the temperature was maintained at 40 ° C., and stirring was performed at a constant speed. Subsequent operations are based on the p of the reaction solution.
The same operation and measurement as in Example 1 were carried out, except that H was kept at 10.5 at all times. As a result, black dried granules of nickel oxyhydroxide coated with a cobalt compound having conductivity were obtained. The resistance was 0.90Ω and the average particle size was 10.5 μm. In addition, the peak coincided with the peak of β-type nickel oxyhydroxide (JCPD
S card number = 60141).

【0014】[0014]

【発明の効果】本発明の表面導電性オキシ水酸化ニッケ
ル製造方法は、pH5〜11の水溶液中で粒状水酸化ニ
ッケルとコバルト塩とを反応させて中間体を得る工程1
と、前記得られた中間体を水溶液中で酸化する工程2と
の2工程からなる簡易な製造方法である。また、本発明
に係る製造方法により得られる表面導電性オキシ水酸化
ニッケルは、表面がコバルト化合物で被覆されているオ
キシ水酸化ニッケルであり、優れた表面導電性を有す
る。なお、Ni−Mn用正極材料として、優れた性能を
発揮する。
According to the process for producing surface-conductive nickel oxyhydroxide of the present invention, a step 1 of reacting granular nickel hydroxide with a cobalt salt in an aqueous solution having a pH of 5 to 11 to obtain an intermediate.
And a step 2 of oxidizing the obtained intermediate in an aqueous solution. The surface-conductive nickel oxyhydroxide obtained by the production method according to the present invention is nickel oxyhydroxide whose surface is coated with a cobalt compound, and has excellent surface conductivity. In addition, it exhibits excellent performance as a positive electrode material for Ni-Mn.

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

【図1】本発明の製造方法により得られる表面導電性オ
キシ水酸化ニッケルの電子顕微鏡写真である。
FIG. 1 is an electron micrograph of a surface conductive nickel oxyhydroxide obtained by the production method of the present invention.

【図2】本発明の製造方法により得られる表面導電性オ
キシ水酸化ニッケルの表面を拡大した電子顕微鏡写真で
ある。
FIG. 2 is an electron micrograph showing an enlarged surface of surface conductive nickel oxyhydroxide obtained by the production method of the present invention.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 飯田 得代志 福井県福井市白方町45字砂浜割5番10 株 式会社田中化学研究所内 Fターム(参考) 4G048 AA04 AB02 AC04 AC06 AE05 AE07 5H050 AA01 BA11 CA03 DA02 DA10 EA01 EA12 FA17 FA18 GA15 GA22 HA10  ────────────────────────────────────────────────── ─── Continuing from the front page (72) Inventor Tokushi Iida 5-10, Sakahama-wari, 45, Shirakata-cho, Fukui-shi, Fukui F-term in Tanaka Chemical Laboratory Co., Ltd. 4G048 AA04 AB02 AC04 AC06 AE05 AE07 5H050 AA01 BA11 CA03 DA02 DA10 EA01 EA12 FA17 FA18 GA15 GA22 HA10

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 pH5〜11の水溶液中で粒状水酸化ニ
ッケルとコバルト塩とを反応させて中間体を得る工程1
と、前記得られた中間体を水溶液中で酸化する工程2と
からなる表面導電性オキシ水酸化ニッケル製造方法。
1. A step 1 of reacting granular nickel hydroxide with a cobalt salt in an aqueous solution having a pH of 5 to 11 to obtain an intermediate.
And a step 2 of oxidizing the obtained intermediate in an aqueous solution.
【請求項2】 前記工程1において、前記pHが9〜1
1の範囲であり、かつ前記水溶液中にアンモニウム塩が
溶解していることを特徴とする請求項1に記載の表面導
電性オキシ水酸化ニッケル製造方法。
2. In the step 1, the pH is 9 to 1.
2. The method for producing a surface conductive nickel oxyhydroxide according to claim 1, wherein the ammonium salt is dissolved in the aqueous solution.
【請求項3】 請求項1または2に記載の製造方法によ
り得られる表面導電性オキシ水酸化ニッケル。
3. A surface conductive nickel oxyhydroxide obtained by the production method according to claim 1.
JP2000181061A 2000-06-16 2000-06-16 Surface conductive nickel oxyhydroxide and method for producing the same Expired - Fee Related JP3505133B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002110154A (en) * 2000-07-14 2002-04-12 Matsushita Electric Ind Co Ltd Manufacturing method of positive pole active material for alkaline battery
WO2002069420A1 (en) * 2001-02-26 2002-09-06 Fdk Corporation Alkaline primary battery
US6991875B2 (en) 2002-08-28 2006-01-31 The Gillette Company Alkaline battery including nickel oxyhydroxide cathode and zinc anode

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6319760A (en) * 1986-07-10 1988-01-27 Japan Storage Battery Co Ltd Nonaqueous electrolyte battery and manufacture of its positive active material
JPH10214622A (en) * 1997-01-30 1998-08-11 Sanyo Electric Co Ltd Sealed alkaline storage battery
JPH11144724A (en) * 1997-11-07 1999-05-28 Japan Storage Battery Co Ltd Non-sintering nickel hydroxide electrode for alkaline storage battery

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6319760A (en) * 1986-07-10 1988-01-27 Japan Storage Battery Co Ltd Nonaqueous electrolyte battery and manufacture of its positive active material
JPH10214622A (en) * 1997-01-30 1998-08-11 Sanyo Electric Co Ltd Sealed alkaline storage battery
JPH11144724A (en) * 1997-11-07 1999-05-28 Japan Storage Battery Co Ltd Non-sintering nickel hydroxide electrode for alkaline storage battery

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002110154A (en) * 2000-07-14 2002-04-12 Matsushita Electric Ind Co Ltd Manufacturing method of positive pole active material for alkaline battery
WO2002069420A1 (en) * 2001-02-26 2002-09-06 Fdk Corporation Alkaline primary battery
US7344803B2 (en) 2001-02-26 2008-03-18 Fdk Corporation Alkaline primary battery
US6991875B2 (en) 2002-08-28 2006-01-31 The Gillette Company Alkaline battery including nickel oxyhydroxide cathode and zinc anode

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