JPS6055A - Manufacture of silver oxide battery - Google Patents

Manufacture of silver oxide battery

Info

Publication number
JPS6055A
JPS6055A JP58107065A JP10706583A JPS6055A JP S6055 A JPS6055 A JP S6055A JP 58107065 A JP58107065 A JP 58107065A JP 10706583 A JP10706583 A JP 10706583A JP S6055 A JPS6055 A JP S6055A
Authority
JP
Japan
Prior art keywords
silver oxide
silver
graphite
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.)
Pending
Application number
JP58107065A
Other languages
Japanese (ja)
Inventor
Yukio Muramatsu
村松 幸男
Kenzo Kawashima
川島 健三
Masatsugu Kondo
近藤 正嗣
Tadashi Sawai
沢井 忠
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP58107065A priority Critical patent/JPS6055A/en
Publication of JPS6055A publication Critical patent/JPS6055A/en
Pending 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
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/54Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of silver
    • 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)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To stabilize internal resistance by reducing the surface of granulated silver oxide powder by spraying reducing solution in hot fluidized air, and forming a positive mix of silver oxide battery with a mixture of the reduced silver oxide and graphite. CONSTITUTION:Granulated silver oxide powder is fluidized in hot fluidized air, and the surface of the powder is reduced by 2-7wt% of the total silver oxide by spraying reducing solution. 1-3wt% graphite is mixed with this silver oxide powder and the mixture is molded in a pellet to form a positive mix 1. The pellet is pressed in a positive case 3, and combined with a negative electrode 6 mainly comprising amalgamated zinc powder, a separator 4, and an absorbing material 4 to form a silver oxide battery. By uniformly convering the surface of granulated silver oxide with metallic silver and mixing with graphite, breakage of silver network is prevented and closed circuit voltage is improved.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、酸化銀電池の製造法、特に、正極活物質の製
造法に関し、顆粒酸化粒子の狭面を還元したものと、黒
鉛とを混合して得られたものを正極活物質として用いる
ことによシ、電池の内部抵抗が安定し更に閉路電圧特性
も安定(−だ優れた酸化銀電池を提供するものである。
[Detailed Description of the Invention] Industrial Field of Application The present invention relates to a method for producing a silver oxide battery, particularly a method for producing a positive electrode active material, in which a reduced narrow side of granular oxide particles is mixed with graphite. By using the obtained material as a positive electrode active material, the internal resistance of the battery is stabilized, and the closed circuit voltage characteristics are also stable (-), thereby providing a silver oxide battery with excellent properties.

従来例の構成とその問題点 従来、酸化銀電池において、内部抵抗を安定させるとい
う目的で、以下の様な提案がなされている。すなわち、
酸化銀粉末を還元して粒子の表面に金属銀層を形成(−
だものをカ6圧成型して正極活物質として構成すること
によって、その金属銀層のネットワークを利用して電池
の内部抵抗を安定させるというものである。1〜がし、
この提案は、次に述べる様な欠点を残している。その欠
点は、酸化銀粉末を還元して粒子の表面に金属銀層を形
成した後、加圧成型してペレットにした時に粒子の表面
に形成されていた金属銀層が破壊きれると、とである。
Conventional configurations and their problems Conventionally, the following proposals have been made for the purpose of stabilizing the internal resistance of silver oxide batteries. That is,
Silver oxide powder is reduced to form a metallic silver layer on the particle surface (-
By forming the battery into a positive electrode active material using six-pressure molding, the internal resistance of the battery can be stabilized using the network of the metallic silver layer. 1~gashi,
This proposal still has the following shortcomings. The drawback is that after reducing the silver oxide powder to form a metallic silver layer on the surface of the particles, the metallic silver layer formed on the surface of the particles is destroyed when the particles are press-molded into pellets. be.

またペレット状に加圧成型した際に、成型金型に酸化銀
やその粒子表面に形成されている金属銀が付着し、ペレ
ットを成型金型から取り出す時ペレットと成型金型との
間のすべりが惑くなシ、ペレットの割れやカケ等の問題
点が生じていた。
In addition, when pressure molding into pellets, silver oxide and metallic silver formed on the particle surface adhere to the mold, and when the pellet is taken out from the mold, slippage occurs between the pellet and the mold. However, there were problems such as cracking and chipping of the pellets.

さらに、そのペレットを正極ケース内に充填して二次加
圧すると、酸化銀粉末の粒子表向に形成されていた金属
銀層が激しく破壊されるために、金属銀層によるネノト
ワ〜りが充分にできず、電池の円部抵抗にバラツキを生
じ、閉路電圧特性にもバラツキを生じていた。また、こ
こでの酸化銀粉末の還元方法は、還元性溶液に酸化銀粉
末を浸漬して酸化銀粒子の表面を還元し金属層を形成す
るという方法であった。しかし、この様な還元方法では
、酸化銀粒子の表面を均一に還元する事が困難であり、
また、還元性溶液に酸化銀を浸漬するため攪拌方法等に
よって、粒子の形状や、粒子表面の金属銀層が破壊され
ることがあった。
Furthermore, when the pellets are filled into the positive electrode case and subjected to secondary pressurization, the metallic silver layer formed on the surface of the silver oxide powder particles is violently destroyed, so that the metallic silver layer does not cause enough distortion. This resulted in variations in the circular resistance of the battery and variations in the closed circuit voltage characteristics. Further, the method for reducing the silver oxide powder here was a method in which the silver oxide powder was immersed in a reducing solution to reduce the surface of the silver oxide particles to form a metal layer. However, with such a reduction method, it is difficult to uniformly reduce the surface of silver oxide particles.
Furthermore, the shape of the particles and the metallic silver layer on the surface of the particles may be destroyed due to the stirring method used to immerse the silver oxide in the reducing solution.

発明の目的 本発明は、以上述べた様な従来の問題点を正極活物質の
還元方法を改め、更に黒鉛を混合することによって解決
し、酸化銀電池の内部抵抗や閉路電圧特性を安定させる
とともに、正極の製造工程を簡略化して生産性の向上を
図ることを目的とする。
Purpose of the Invention The present invention solves the conventional problems described above by modifying the reduction method of the positive electrode active material and further mixing graphite, thereby stabilizing the internal resistance and closed circuit voltage characteristics of the silver oxide battery. The purpose is to simplify the manufacturing process of positive electrodes and improve productivity.

発明の構成 本発明は上記目的を達成するため、顆粒状酸化銀を加温
した流動空気中で流動状態とj−1この流動状態の酸化
銀に還元性溶液を噴霧1〜で粒子表面を還元し、これと
黒鉛とを混合し、たものを正極合剤と(−で用いること
を特徴としたものである。
Structure of the Invention In order to achieve the above object, the present invention aims to reduce the particle surface by reducing the particle surface by reducing the particle surface by spraying a reducing solution onto the silver oxide in the fluidized state in a fluidized state in heated fluidized air. This is characterized in that it is mixed with graphite and used as a positive electrode mixture (-).

実施例の説明 以下、本発明の詳細な説明する。第1図は本発明の実施
例における酸化銀電池の半断面図である。
DESCRIPTION OF EMBODIMENTS The present invention will now be described in detail. FIG. 1 is a half-sectional view of a silver oxide battery in an example of the present invention.

1は本発明による正極合剤であり、顆粒状酸化銀粒子の
表面を還元性溶液で還元したものと黒鉛を混合したもの
を加圧成型してなるものである。2は断面り字状の正極
リングで、正極合剤の肩部を保護しかつ封口圧力を受け
止める役割をするものである。3は正極端子を兼ねた正
極ケース、4はポリエチレンから成る微孔性フィルムと
セロファンとから成るセパレータ、6はナイロン不織布
、あるいはセルロースやコノトン等から成る電解液含浸
材、6は負極で水化亜鉛粉末とカルボキシメチルセルロ
ース等の造粘剤及びアルカリ電解液から構成されている
。7は負極端子を兼ねた封目板、8は封ロバノキングで
、一般的にはナイロン66゜11等から成っている。こ
のような構成の電池において、正極合剤1は、顆粒状酸
化銀の粒子の表面を還元性溶液を用いて還元する際に、
加温した流動空気中で流動状態にし、流動状態にした酸
化銀に還元性溶液を噴霧して表面を還元し、同時に乾燥
を行ない顆粒状酸化銀粒子の表面に金属銀層を形成した
ものを用いた。酸化銀の還元量は酸化銀総量の2〜7重
量パーセントとし、2〜7重量パーセントの還元に相当
する還元性溶液を噴霧する。表面を金属銀化した正極活
物質と黒鉛とを混合した合剤をペレット状に成型して用
いる。以下、本発明の特徴とする正極活物質の製造法に
ついて詳細に説明する。第2図に示す流動槽11内に顆
粒状酸化銀を投入し、槽下部の吹き込み口12より乾燥
した空気を吹き込んで上方に吹き上げ、顆粒状酸化銀を
攪拌する。一方これとは別にあらかじめヒドラジン等の
還元性溶液を酸化銀の還元量が2〜7重量パーセントと
なるように秤量し、メチルアルコール等の溶媒で希釈し
ておく。メチルアルコール等の溶媒で希釈L−だヒドラ
ジン等の還元性溶液13を14に示すノズルより流動槽
内にスプレー状に噴霧する。スプレー状に噴霧された還
元性溶液は、流動槽内で乾燥した空気によI)攪拌され
ている顆粒状酸化銀の表面と接触し、その表面層を還元
して顆粒状酸化銀の表面は金属銀化する。流動槽内では
、あらかじめ乾燥した空気が吹き上げられているため、
還元反応と同時に乾燥が行なわれ、短時間で表面層を均
一に金属銀で覆った正極活物質を得ることがで、きる。
1 is a positive electrode mixture according to the present invention, which is made by pressure molding a mixture of granular silver oxide particles whose surfaces have been reduced with a reducing solution and graphite. Reference numeral 2 denotes a positive electrode ring having an angular cross-section, which serves to protect the shoulder of the positive electrode mixture and to absorb sealing pressure. 3 is a positive electrode case that also serves as a positive electrode terminal, 4 is a separator made of a microporous film made of polyethylene and cellophane, 6 is an electrolyte-impregnated material made of nylon nonwoven fabric or cellulose or conoton, etc., and 6 is a negative electrode made of zinc hydrate. It consists of powder, a thickening agent such as carboxymethyl cellulose, and an alkaline electrolyte. 7 is a sealing plate which also serves as a negative electrode terminal, and 8 is a sealing robber king, which is generally made of nylon 66°11 or the like. In a battery having such a configuration, when the positive electrode mixture 1 reduces the surface of the granular silver oxide particles using a reducing solution,
Silver oxide particles are made into a fluidized state in heated fluidized air, the surface is reduced by spraying a reducing solution onto the fluidized silver oxide particles, and at the same time, a metallic silver layer is formed on the surface of the granular silver oxide particles. Using. The amount of silver oxide reduced is 2 to 7 percent by weight of the total amount of silver oxide, and a reducing solution corresponding to a reduction of 2 to 7 percent by weight is sprayed. A mixture of a positive electrode active material whose surface is made of metallic silver and graphite is molded into pellets and used. Hereinafter, a method for producing a positive electrode active material, which is a feature of the present invention, will be explained in detail. Granular silver oxide is placed in a fluidized tank 11 shown in FIG. 2, and dry air is blown upward from the blowing port 12 at the bottom of the tank to stir the granular silver oxide. Separately from this, a reducing solution such as hydrazine is weighed in advance so that the amount of silver oxide reduced is 2 to 7% by weight, and diluted with a solvent such as methyl alcohol. A reducing solution 13 such as L-hydrazine diluted with a solvent such as methyl alcohol is sprayed into the fluidized tank through a nozzle 14. The sprayed reducing solution comes into contact with the surface of the granular silver oxide which is being stirred by dry air in the fluidized tank, reducing the surface layer and reducing the surface of the granular silver oxide. Silverizes metal. Because dry air is blown up in the fluidized tank,
Drying is performed simultaneously with the reduction reaction, and a positive electrode active material whose surface layer is uniformly covered with metallic silver can be obtained in a short time.

なお16は排気口である。Note that 16 is an exhaust port.

この方法で得た正極活物質と黒鉛とを混合した合剤をペ
レット状に加圧成型した後、正極ケースに充填し、二次
加圧する。上記の製造法で得た正極活物質と黒鉛とを混
合した合剤を用いた正極を、ペレット状に加圧成型し、
正極ケースで二次加圧した際には、顆粒状酸化銀の界面
に形成された金属銀層のネットワークが破壊されるが、
黒鉛が酸化銀総重量の最低1重量パーセント以上混合さ
れていれば、金属銀層のネットワークの破壊された部分
をカバーし、充分な導電性を得ることができる。
The mixture of the positive electrode active material and graphite obtained by this method is press-molded into a pellet shape, then filled into a positive electrode case and subjected to secondary pressurization. A positive electrode using a mixture of the positive electrode active material obtained by the above manufacturing method and graphite is press-molded into a pellet shape,
When secondary pressure is applied in the positive electrode case, the network of metallic silver layer formed at the interface of granular silver oxide is destroyed;
If graphite is mixed in an amount of at least 1% by weight based on the total weight of silver oxide, it is possible to cover the destroyed portions of the network of the metallic silver layer and obtain sufficient conductivity.

また黒鉛の滑性によりペレット状に加圧成型した際に、
成型金型に酸化銀や、その粒子表面に形成されている金
属銀が付着することもなく、ペレットを成型金型から取
り出す時、ペレットと成型金型との間のすべりも良く、
従来のペレットの割れやカケ等の問題も解消できる。
In addition, due to the slipperiness of graphite, when press-molded into pellets,
Silver oxide and metallic silver formed on the particle surface do not adhere to the mold, and when the pellet is taken out of the mold, there is good slippage between the pellet and the mold.
Problems such as cracking and chipping of conventional pellets can also be solved.

黒鉛の添刀口量が酸化銀総量の3重量パーセント以上に
なると正極合剤のかさが高くなって、高密度の正極を得
られなくなるため不利になる。さらに、顆粒状酸化銀の
還元量については、種々の検討を行なっ/Cが、電池と
しての優れた内部抵抗や閉路電圧特性を得るためには、
少なくとも酸化銀総重量の2重量パーセント以上還元す
る必要があり、逆に7重量パーセントを超す還元量を施
すと、活物質としての酸化銀の有効添加量を減少させる
ことになり不利になる。
If the amount of graphite added exceeds 3% by weight of the total amount of silver oxide, the bulk of the positive electrode mixture increases, making it impossible to obtain a high-density positive electrode, which is disadvantageous. Furthermore, various studies were conducted regarding the amount of reduction of granular silver oxide, and in order to obtain excellent internal resistance and closed circuit voltage characteristics as a battery,
It is necessary to reduce at least 2% by weight of the total weight of silver oxide; conversely, if the amount of reduction exceeds 7% by weight, the effective amount of silver oxide added as an active material will be reduced, which is disadvantageous.

以下、本発明による具体例を説明する。ここで用いた本
発明の製造法による正極の構成条件は、次の通りである
Hereinafter, specific examples according to the present invention will be explained. The configuration conditions of the positive electrode according to the manufacturing method of the present invention used here are as follows.

1 還元量・・・・・・酸化銀総量の6重量パーセント
1. Reduction amount: 6% by weight of the total amount of silver oxide.

2 黒鉛の添加量・・・・・酸化銀総量の2重量パーセ
ント。
2 Added amount of graphite: 2% by weight of the total amount of silver oxide.

以上の構成条件で製造した正極を用いた電池をA1還元
量と黒鉛の添加量がそれぞれ酸化銀総量の51iffi
バーセントと0重量パーセントのものを正極として用い
た電池をB1同じく6重量パーセントと4重量パーセン
トのものを正極として用いた電池を01同じく1重量パ
ーセントと2重量パーセントのものを正極として用いた
電池をB1同じく8重量パーセントと2重量パーセント
のものを正極として用いた電池をE1従来の酸化銀粉末
を還元性溶液に浸漬して酸化銀粒子の表面を還元し金属
銀層を形成したものを正極として用いた電池をFとした
。なお電池Fの酸化銀還元量は、酸化銀総量の5重量パ
ーセントとした。以上の条件で製造した電池A、B、C
,D、F、、Fのペレツト割れの数量と初期閉路電圧及
び放電容量を次表に示す。なおここで比較試験に用いた
電池サイズは、直径7.9mm、高さ2.1咽の酸化銀
電池R8721SW である。
In a battery using the positive electrode manufactured under the above configuration conditions, the amount of A1 reduction and the amount of graphite added were each 51iffi of the total amount of silver oxide.
B1: A battery using 6% and 4% by weight as the positive electrode; 01: A battery using 1% and 2% by weight as the positive electrode. B1 A battery using the same 8 weight percent and 2 weight percent as the positive electrode.E1 A battery using conventional silver oxide powder immersed in a reducing solution to reduce the surface of the silver oxide particles and form a metallic silver layer as the positive electrode. The battery used was F. The amount of silver oxide reduced in Battery F was 5% by weight of the total amount of silver oxide. Batteries A, B, and C manufactured under the above conditions
The number of pellet cracks, initial closing voltage, and discharge capacity of ,D,F,,F are shown in the following table. The battery size used in the comparative test here was a silver oxide battery R8721SW with a diameter of 7.9 mm and a height of 2.1 mm.

前表に示した各項目の測定条件は次の通りである。The measurement conditions for each item shown in the previous table are as follows.

ペレット割れ・・・・・・n=60の製造時のペレット
割れ個数。
Pellet cracking: Number of pellets cracked during production of n=60.

閉路電圧・・・・・各温度条件に16時間放置後、2に
Ω、5秒間の最低電圧を測定し、n−6の平均値。
Closed circuit voltage: After being left in each temperature condition for 16 hours, the lowest voltage was measured at 2Ω for 5 seconds, and the average value of n-6.

放電容量・・・・20℃における30にΩ定抵抗放電で
終止電圧1.4■までの放電時間より算出したもので、
n=5の平均値。
Discharge capacity: Calculated from the discharge time to the final voltage of 1.4μ with a constant resistance discharge of 30Ω at 20°C.
Average value of n=5.

以上の結果より、電池B、D、Fはペレット割れという
問題があり、電池C,Eは容量が少ないという結果であ
る。
From the above results, batteries B, D, and F had the problem of pellet cracking, and batteries C and E had a small capacity.

発明の効果 以上の通シ、本発明の製造法で得た電池は、ペレット割
れがなく、放電容量が大きいとともに閉路電圧も充分で
ある。
In addition to the effects of the invention, the battery obtained by the manufacturing method of the invention has no pellet cracking, has a large discharge capacity, and has a sufficient closed circuit voltage.

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

11・・・・・・流動槽、12・・・・加熱(〜た望見
の吹き込み口、13・・・・・・還元性溶液、14・・
・・スプレーノズル。
11...Fluidization tank, 12...Heating (~tai no inlet), 13...Reducing solution, 14...
··spray nozzle.

Claims (3)

【特許請求の範囲】[Claims] (1)顆粒状酸化銀を加温した流動空気中で流動状態と
し、この酸化銀に還元性溶液を噴霧してその粒子表面を
還元したものと、黒鉛とを混合したものを正極合剤とし
て用いることを特徴とする酸化銀電池の製造法。
(1) Granular silver oxide is brought into a fluidized state in heated fluidized air, and a reducing solution is sprayed onto the silver oxide to reduce the particle surface. A mixture of this and graphite is used as a positive electrode mixture. A method for manufacturing a silver oxide battery, characterized in that it is used.
(2)還元して得だ金属銀が酸化銀総量の2〜7重量パ
ーセントである特許請求の範囲第1項記載の酸化銀電池
の製造法。
(2) The method for producing a silver oxide battery according to claim 1, wherein the metallic silver obtained by reduction is 2 to 7 weight percent of the total amount of silver oxide.
(3)黒鉛の添加量が1〜3重量パーセントである特許
請求の範囲第1項記載の酸化銀電池の製造法。
(3) The method for producing a silver oxide battery according to claim 1, wherein the amount of graphite added is 1 to 3 weight percent.
JP58107065A 1983-06-15 1983-06-15 Manufacture of silver oxide battery Pending JPS6055A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58107065A JPS6055A (en) 1983-06-15 1983-06-15 Manufacture of silver oxide battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58107065A JPS6055A (en) 1983-06-15 1983-06-15 Manufacture of silver oxide battery

Publications (1)

Publication Number Publication Date
JPS6055A true JPS6055A (en) 1985-01-05

Family

ID=14449593

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58107065A Pending JPS6055A (en) 1983-06-15 1983-06-15 Manufacture of silver oxide battery

Country Status (1)

Country Link
JP (1) JPS6055A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004073095A1 (en) * 2003-02-13 2004-08-26 Dowa Mining Co., Ltd. Silver oxide powder for alkali battery and process for producing the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004073095A1 (en) * 2003-02-13 2004-08-26 Dowa Mining Co., Ltd. Silver oxide powder for alkali battery and process for producing the same
AU2004211104B2 (en) * 2003-02-13 2009-01-29 Dowa Mining Co., Ltd. Silver oxide powder for alkaline battery and method of producing the same
AU2004211104C1 (en) * 2003-02-13 2009-08-13 Dowa Mining Co., Ltd. Silver oxide powder for alkaline battery and method of producing the same
US7771872B2 (en) 2003-02-13 2010-08-10 Dowa Electronics Materials Co., Ltd. Silver oxide powder for alkaline battery and method of producing the same

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