JPH02276156A - Manufacture of organic electrolyte battery - Google Patents

Manufacture of organic electrolyte battery

Info

Publication number
JPH02276156A
JPH02276156A JP1096792A JP9679289A JPH02276156A JP H02276156 A JPH02276156 A JP H02276156A JP 1096792 A JP1096792 A JP 1096792A JP 9679289 A JP9679289 A JP 9679289A JP H02276156 A JPH02276156 A JP H02276156A
Authority
JP
Japan
Prior art keywords
positive electrode
mixture
positive
mix
binder
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
JP1096792A
Other languages
Japanese (ja)
Other versions
JPH0760678B2 (en
Inventor
Hideo Sakamoto
秀夫 坂本
Kensuke Tawara
謙介 田原
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.)
Seiko Electronic Components Ltd
Original Assignee
Seiko Electronic Components 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 Seiko Electronic Components Ltd filed Critical Seiko Electronic Components Ltd
Priority to JP1096792A priority Critical patent/JPH0760678B2/en
Publication of JPH02276156A publication Critical patent/JPH02276156A/en
Publication of JPH0760678B2 publication Critical patent/JPH0760678B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture
    • 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
    • H01M4/483Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides for non-aqueous cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To increase the fluidity of a positive mix, to make molding by rubbing weighing passible, and to increase binding capability of a positive pellet in low density molding to prevent coming off or breakage of the mix by using the positive mix prepared by granulating, then adding a binder thereto. CONSTITUTION:Bismuth trioxide powder serving as a positive active material and carbon conductor are mixed, and molded in tablets, then the tablets are crushed to form granules. Granulated mix 1 and a binder 2 comprising a fluororesin emersion are mixed and the mixture is dried, then passed through screens to form a positive mix. This positive mix has narrow weight dispersion in molding by rubbing weighing. Pellet strength required for assembly and hadling is made high, and handling is also made easy.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、リチウムを負極主活物質とし、三酸化ビスマ
スを正極主活物質とする有機電解質電池の正極の製造方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a positive electrode for an organic electrolyte battery in which lithium is used as a negative electrode main active material and bismuth trioxide is used as a positive electrode main active material.

〔発明の概要〕[Summary of the invention]

本発明は、リチウムを生活物質とする負極と、有機電解
液と、三酸化ビスマスを生活物質とする正極とから成り
、加圧成形後の正極ペレットを低密度充填とする有機電
解質電池に於いて、正極合剤を造粒することによって、
正極合剤の流動性を高めてスリキリ秤量による成形を可
能とし、更に造粒した粒子表面に結着性を付着させる事
により低密度充填の正極ペレットの結着性を高めて搬送
時や組立時等々での合剤の脱落や崩れを抑制し、取り扱
いの容易な正極ペレットを提供するものである。
The present invention is an organic electrolyte battery comprising a negative electrode containing lithium as a living material, an organic electrolyte, and a positive electrode containing bismuth trioxide as a living material, and in which the positive electrode pellets after pressure molding are packed at a low density. , by granulating the positive electrode mixture,
By increasing the fluidity of the positive electrode mixture, it is possible to form it by precise weighing, and by attaching binding properties to the surface of the granulated particles, the binding properties of the low-density packed positive electrode pellets are increased during transportation and assembly. The object is to provide a positive electrode pellet that is easy to handle by suppressing the mixture from falling off or collapsing due to the above-mentioned conditions.

〔従来の技術〕[Conventional technology]

従来、この種の電池において、例えばボタン型電池を製
造する場合、正極は次のように作られていた。即ち活物
質である三酸化ビスマスとグラファイトやカーボンブラ
ック等の炭素粉末又は金属粉末等の導電剤、およびフッ
素樹脂やポリスチレン等の樹脂結着剤を所定組成比で混
合し、次にこの正極合剤の所定量を成型機の金型内に充
填し、正極保持リングと共に加圧成形することによって
正極ペレットとする。こうして得られた正極ペレットは
減圧加熱乾燥され充分脱水された後、正極缶に組み込ま
れて電池に組み立てられていた。正極合剤の所定量を成
型機の金型内に充填する方法として、底部に合剤の落下
する穴を有する容器(フィーダ)に合剤を充填して、金
型上を往復させる、もしくは金型が移動して、金型内に
合剤を充填するスリキリ秤量が広く行われている。
Conventionally, in this type of battery, for example, when manufacturing a button-type battery, the positive electrode was made as follows. That is, the active material bismuth trioxide, a conductive agent such as carbon powder or metal powder such as graphite or carbon black, and a resin binder such as fluororesin or polystyrene are mixed in a predetermined composition ratio, and then this positive electrode mixture is mixed. A predetermined amount of the material is filled into a mold of a molding machine, and the mixture is press-molded together with a positive electrode holding ring to form positive electrode pellets. The thus obtained positive electrode pellets were thoroughly dehydrated by heating and drying under reduced pressure, and then incorporated into a positive electrode can and assembled into a battery. A method for filling a predetermined amount of positive electrode mixture into the mold of a molding machine is to fill a container (feeder) with a hole in the bottom for the mixture to fall into and move it back and forth over the mold, or Scrap weighing, in which the mold is moved and the mixture is filled into the mold, is widely used.

又、この種の電池を放電させた場合、放電の進行に伴い
負極リチウムの体積は減少し、正極は膨張する。しかし
、負極リチウムの体積減少以上に正極が膨張するので電
池総厚を高くして、甚だしい場合には使用機器を破壊し
てしまう。この為、正極ペレットを低密度充填して正極
の膨張を抑制する方法が行われており、この場合、組立
時の取扱いやペレットの強度アップの為に正極保持リン
グが使われている。
Furthermore, when this type of battery is discharged, the volume of the negative electrode lithium decreases and the positive electrode expands as the discharge progresses. However, since the positive electrode expands more than the volume reduction of the negative electrode lithium, the total thickness of the battery increases, and in extreme cases, the equipment used may be destroyed. For this reason, a method is used to suppress the expansion of the positive electrode by packing the positive electrode pellets at a low density, and in this case, a positive electrode holding ring is used for handling during assembly and for increasing the strength of the pellets.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかし、前述の様にして作られた正極合剤の所定量を、
スリキリ秤量により成型機の金型内に充填する際、合剤
の流動性が悪い為充填量のバラツキが大きく、加圧成形
後に正極ペレットの重量選別を行う等の作業性の低下、
又、合剤の充填ムラにより正極ペレットのカケや合剤の
脱落が生じ正極容量が減少する、正極ペレットの厚みが
不均一になり封止性が低下するという問題があった。
However, when the predetermined amount of the positive electrode mixture prepared as described above is
When filling the mold of a molding machine using a pick-up weighing method, the fluidity of the mixture is poor, resulting in large variations in the amount of filling, resulting in reduced work efficiency, such as having to sort out the weight of the positive electrode pellets after pressure molding.
In addition, due to uneven filling of the mixture, the positive electrode pellets may chip or the mixture may fall off, resulting in a decrease in positive electrode capacity, and the thickness of the positive electrode pellets may become non-uniform, resulting in a decrease in sealing performance.

又、合剤の流動性を向上させる為に合剤を造粒する等な
どの方法があるが、低密度で正極ペレットの成形を行う
場合には正極ペレットの結着性が弱い為、成形後の取扱
い等で造粒した粒子の脱落や甚だしい場合には正極ペレ
ットの崩れが生じるという問題があった。
In addition, there are methods such as granulating the mixture to improve the fluidity of the mixture, but when molding positive electrode pellets at low density, the cohesiveness of the positive electrode pellets is weak, so There is a problem in that the granulated particles fall off during handling, and in severe cases, the positive electrode pellets collapse.

〔課題を解決するための手段〕[Means to solve the problem]

上記のような問題点を解決するため、本発明者等は種々
検討した結果、正極合剤を予め造粒し、整粒した後、結
着剤を添加した正極合剤を用いることを提起するもので
ある。
In order to solve the above-mentioned problems, the present inventors have conducted various studies and proposed to use a positive electrode mixture in which a binder is added after the positive electrode mixture is granulated in advance and sized. It is something.

即ち、正極合剤を造粒し、整粒することにより正極合剤
の流動性を高めて、スリキリ秤量による成形を可能とし
、更に粒子表面に付着した結着剤で、低密度充填の正極
ペレットの結着性を高めて合剤の脱落や崩れを抑制し、
取り扱いの容易な正極ペレットを提供するものである。
In other words, by granulating and sizing the positive electrode mixture, the fluidity of the positive electrode mixture is increased, making it possible to form it by scraping weighing, and furthermore, with the binder attached to the particle surface, it is possible to form positive electrode pellets with low density filling. Improves the binding properties of the mixture to prevent it from falling off or crumbling,
This provides a positive electrode pellet that is easy to handle.

なお、結着剤の添加量を多くすると正極合剤の流動性が
低下するので添加量は重量比1.0%以下が望ましい。
Note that if the amount of the binder added is increased, the fluidity of the positive electrode mixture will decrease, so the amount added is preferably 1.0% or less by weight.

〔作用〕[Effect]

予め結着剤以外の正極合剤を混合造粒し、整粒した後、
水もしくは有機溶媒に分散もしくは溶解した結着剤を添
加することにより結着剤は乾燥状態に添加する場合に比
べて結着剤が造粒粒子に強く結合する為、乾燥後の合剤
粒子に微粉が少なく粒子の流動性が高い。この為スリキ
リ秤量精度が著しく向上する。又、正極ペレットの結着
性が高くなるのは、正極合剤を造粒後、水もしくは有機
溶媒等の液体に分散もしくは溶解した結着剤を添加する
ことにより、結着剤を粉末等の乾燥状態で添加する場合
に比べて、粒子表面への結着剤の付着が充分におこなわ
れて、ペレット成形後の粒子同志の結着力が高くなるこ
とによると考えられる。
After pre-mixing and granulating the positive electrode mixture other than the binder and sizing,
By adding a binder dispersed or dissolved in water or an organic solvent, the binder binds to the granulated particles more strongly than when it is added in a dry state, so There is little fine powder and the particles have high fluidity. For this reason, the accuracy of pick-up weighing is significantly improved. In addition, the binding properties of positive electrode pellets can be increased by adding a binder dispersed or dissolved in a liquid such as water or an organic solvent after granulating the positive electrode mixture. This is thought to be due to the fact that, compared to the case where the binder is added in a dry state, the binder is sufficiently attached to the particle surface, and the binding force between the particles after pellet formation is increased.

更に正極保持リングを用いることにより、取り扱いのよ
り容易な正極ペレットを提供することができた。
Furthermore, by using a positive electrode holding ring, it was possible to provide a positive electrode pellet that was easier to handle.

〔実施例〕〔Example〕

以下、実施例により本発明をさらに詳細に説明する。 Hereinafter, the present invention will be explained in more detail with reference to Examples.

〔実施例1〕 本実施例では正極合剤を次のようにして作製した。正極
活物質として二酸化ビスマス粉末と炭素導電剤(グラフ
ァイトまたは/およびカーボンブラック)とを、重量比
96:4の割合で混合し打錠成型を行った後に砕いて6
0〜100メツシユの篩を通して整粒した。次にこの整
粒合剤とフッ素樹脂エマルジョンからなる結着剤とを重
量比99.8:0.2(正味のフッ素樹脂重量)の割合
で混合し、60℃で10時間乾燥した後、篩を通して3
2〜100メツシユの正極合剤(A)とした。なおフッ
素樹脂エマルジョンは正極合剤の重量の1/10の蒸留
水で希釈したものを用い、フッ素樹脂の正味の添加量が
0,2重量%となるようにした。この時の正極合剤(A
)の収率は97%であった。
[Example 1] In this example, a positive electrode mixture was prepared as follows. Bismuth dioxide powder and a carbon conductive agent (graphite or/and carbon black) are mixed as a positive electrode active material at a weight ratio of 96:4, and the mixture is compressed into tablets and crushed into 6
The particles were sized through a sieve with a mesh size of 0 to 100. Next, this sized mixture and a binder made of a fluororesin emulsion were mixed at a weight ratio of 99.8:0.2 (net fluororesin weight), dried at 60°C for 10 hours, and then sieved. through 3
A positive electrode mixture (A) having 2 to 100 meshes was prepared. The fluororesin emulsion was diluted with 1/10 of the weight of the positive electrode mixture in distilled water, so that the net amount of fluororesin added was 0.2% by weight. At this time, the positive electrode mixture (A
) yield was 97%.

又、従来例として、実施例で用いた同じ二酸化ビスマス
粉末と炭素導電剤と蒸留水で希釈したフッ素樹脂エマル
ジョンからなる結着剤とを重量比95、8:4:0. 
2 (正味のフッ素樹脂重量)の割合で混合し、60℃
で10時間乾燥した後、篩を通して32〜100メツシ
ユの正極合剤(B)とした。この時の正極合剤(B)の
収率は55%であった。第1図は本発明の正極合剤(A
)の粒子の模式図である。図において1は二酸化ビスマ
スと炭素導電剤とからなる粒子、2はフッ素樹脂からな
る結着剤で粒子表面に付着している。
Further, as a conventional example, the same bismuth dioxide powder used in the example, a carbon conductive agent, and a binder consisting of a fluororesin emulsion diluted with distilled water were mixed in a weight ratio of 95, 8:4:0.
2 (net fluororesin weight) and heated at 60°C.
After drying for 10 hours, the mixture was passed through a sieve to obtain a positive electrode mixture (B) having 32 to 100 meshes. The yield of positive electrode mixture (B) at this time was 55%. Figure 1 shows the positive electrode mixture (A) of the present invention.
) is a schematic diagram of particles. In the figure, 1 is a particle made of bismuth dioxide and a carbon conductive agent, and 2 is a binder made of a fluororesin, which is attached to the particle surface.

この様にして作製した正極合剤(ASB)を用いて、ス
リキリ秤量による成形によって第2図に示す形状の正極
ベレットを作製した。図において3は正極合剤、4はS
US製の断面逆り字状の正極保持リングであり、金型内
に正極保持リングをL字状に載置した後、正極合剤の所
定量をスリキリ秤量により充填して一体に加圧成形した
ものである。合剤の充填ムラや成形後の合剤脱落、カケ
は正極合剤(A)では見られなかった。
Using the thus prepared positive electrode mixture (ASB), a positive electrode pellet having the shape shown in FIG. 2 was produced by molding by scraping weighing. In the figure, 3 is the positive electrode mixture, 4 is S
This is a positive electrode holding ring made in the US with an inverted cross-section. After placing the positive electrode holding ring in an L-shape in a mold, a predetermined amount of positive electrode mixture is filled using a surikiri weighing method and then pressure molded into one piece. This is what I did. No uneven filling of the mixture, falling off of the mixture after molding, or chipping was observed in the positive electrode mixture (A).

正極ペレットの重量測定結果を第1表に示す。Table 1 shows the weight measurement results of the positive electrode pellets.

尚、重量は正極保持リングを除く重量であり、測定数量
は各200個である。
Note that the weight is the weight excluding the positive electrode holding ring, and the number of pieces measured was 200 each.

第1表 第1表から明らかな様に、合剤を予め造粒し、整粒した
後、粒子表面に結着剤を付着した本発明の正極合剤(A
)を用いた正極ペレットAの重量バラツキは、従来の正
極合剤(B)を用いた正極ペレットAより著しく小さい
。又、正極合剤の収率も著しく優れている。
Table 1 As is clear from Table 1, the positive electrode mixture of the present invention (A
) The weight variation of the positive electrode pellet A using the conventional positive electrode mixture (B) is significantly smaller than that of the positive electrode pellet A using the conventional positive electrode mixture (B). Moreover, the yield of the positive electrode mixture is also extremely excellent.

〔実施例2〕 本実施例では正極合剤を次のようにして作製した。実施
例1で用いたと同じ二酸化ビスマス粉末と炭素導電剤(
グラファイトまたは/およびカーボンブラック)とを、
実施例1と同様に造粒し、整粒し60〜100メツシユ
の粒子とした。次にこの整粒合剤と実施例1で用いたと
同じフッ素樹脂エマルジョンからなる結着剤とを重量比
99゜4:0.6の割合で混合した後、実施例1と同様
に整粒し32〜100メツシユの正極合剤(C)゛とし
た。なお結着剤の添加は実施例1と同じ方法で行った。
[Example 2] In this example, a positive electrode mixture was prepared as follows. The same bismuth dioxide powder and carbon conductive agent (
graphite or/and carbon black),
It was granulated and sized in the same manner as in Example 1 to obtain particles of 60 to 100 meshes. Next, this sized mixture and a binder made of the same fluororesin emulsion as used in Example 1 were mixed at a weight ratio of 99°4:0.6, and then sized in the same manner as in Example 1. The positive electrode mixture (C) had a mesh size of 32 to 100. Note that the binder was added in the same manner as in Example 1.

又、従来例として、実施例1で用いたと同じ二酸化ビス
マス粉末と炭素導電剤と蒸留水で希釈したフッ素樹脂エ
マルジョンとを重量比95.4:4:0.6の割合で混
合し、実施例1の従来例と同様にして正極合剤(D)を
作製した。
In addition, as a conventional example, the same bismuth dioxide powder used in Example 1, a carbon conductive agent, and a fluororesin emulsion diluted with distilled water were mixed in a weight ratio of 95.4:4:0.6. A positive electrode mixture (D) was prepared in the same manner as in Conventional Example 1.

この様にして作製した正極合剤(CSD)を用いてスリ
キリ秤量により正極合剤の所定量を金型内に充填し、加
圧成形を行って正極ペレットC1Dとした。正極ペレッ
トC,Dのfiltバラツキを測定した結果は実施例1
とほとんど同じ傾向で、正極ペレットCの重量バラツキ
が著しく小さかった。
Using the thus produced positive electrode mixture (CSD), a predetermined amount of the positive electrode mixture (CSD) was filled into a mold by scrape weighing, and pressure molding was performed to obtain positive electrode pellets C1D. The results of measuring the filt variations of positive electrode pellets C and D are shown in Example 1.
Almost the same trend was observed, and the weight variation of positive electrode pellet C was extremely small.

〔発明の効果〕〔Effect of the invention〕

以上詳述した様に、合剤を予め造粒した後、粒子表面に
結着剤を付着した本発明の正極合剤は、スリキリ秤量に
よる成形での重量バラツキが小さく、又、組立、搬送等
において必要なベレット強度が高く、取り扱いも容易に
なる等の優れた効果を有する。
As described in detail above, the positive electrode mixture of the present invention, in which a binder is attached to the particle surface after granulating the mixture in advance, has small weight variations when molded by slip-weighing, and is easy to assemble, transport, etc. It has excellent effects such as high pellet strength required in the process and ease of handling.

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

第1図は本発明にかかる正極合剤の粒子の模式図、第2
図は本発明にかかる正極ペレットの一例を示す断面図で
ある。 ・正極合剤粒子 ・結着剤 ・正極合剤 ・正極保持リング 出願人 セイコー電子部品株式会社
FIG. 1 is a schematic diagram of particles of the positive electrode mixture according to the present invention, and FIG.
The figure is a sectional view showing an example of a positive electrode pellet according to the present invention.・Positive electrode mixture particles ・Binder ・Positive electrode mixture ・Positive electrode holding ring Applicant: Seiko Electronic Components Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] リチウムを主活物質とする負極と、有機電解質と、三酸
化ビスマスBi_2O_3を主活物質とする正極とから
少なくとも成る有機電解質電池に於いて、前記正極とし
て三酸化ビスマスと導電剤等々とを混合して予め造粒し
、整粒した後、水もしくは有機溶媒に分散もしくは溶解
した高分子結着剤を添加し、乾燥した正極合剤を用いた
ことを特徴とする有機電解質電池の製造方法。
In an organic electrolyte battery comprising at least a negative electrode having lithium as the main active material, an organic electrolyte, and a positive electrode having bismuth trioxide Bi_2O_3 as the main active material, bismuth trioxide and a conductive agent are mixed as the positive electrode. A method for producing an organic electrolyte battery, characterized in that the positive electrode mixture is granulated in advance, sized, added with a polymer binder dispersed or dissolved in water or an organic solvent, and dried.
JP1096792A 1989-04-17 1989-04-17 Method for manufacturing organic electrolyte battery Expired - Lifetime JPH0760678B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1096792A JPH0760678B2 (en) 1989-04-17 1989-04-17 Method for manufacturing organic electrolyte battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1096792A JPH0760678B2 (en) 1989-04-17 1989-04-17 Method for manufacturing organic electrolyte battery

Publications (2)

Publication Number Publication Date
JPH02276156A true JPH02276156A (en) 1990-11-13
JPH0760678B2 JPH0760678B2 (en) 1995-06-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP1096792A Expired - Lifetime JPH0760678B2 (en) 1989-04-17 1989-04-17 Method for manufacturing organic electrolyte battery

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JP (1) JPH0760678B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62128443A (en) * 1985-11-28 1987-06-10 Toppan Printing Co Ltd Manufacture of electrode for battery

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62128443A (en) * 1985-11-28 1987-06-10 Toppan Printing Co Ltd Manufacture of electrode for battery

Also Published As

Publication number Publication date
JPH0760678B2 (en) 1995-06-28

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