JPH0760678B2 - Method for manufacturing organic electrolyte battery - Google Patents

Method for manufacturing organic electrolyte battery

Info

Publication number
JPH0760678B2
JPH0760678B2 JP1096792A JP9679289A JPH0760678B2 JP H0760678 B2 JPH0760678 B2 JP H0760678B2 JP 1096792 A JP1096792 A JP 1096792A JP 9679289 A JP9679289 A JP 9679289A JP H0760678 B2 JPH0760678 B2 JP H0760678B2
Authority
JP
Japan
Prior art keywords
positive electrode
particles
mixture
binder
organic electrolyte
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP1096792A
Other languages
Japanese (ja)
Other versions
JPH02276156A (en
Inventor
秀夫 坂本
謙介 田原
Original Assignee
セイコー電子部品株式会社
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Filing date
Publication date
Application filed by セイコー電子部品株式会社 filed Critical セイコー電子部品株式会社
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

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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
    • 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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  • 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)

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。
The present invention relates to a method for producing a positive electrode of an organic electrolyte battery using lithium as a negative electrode main active material and bismuth trioxide as a positive electrode main active material.

〔発明の概要〕[Outline of Invention]

本発明は、リチウムを主活物質とする負極と、有機電解
液と、三酸化ビスマスを主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 relates to an organic electrolyte battery comprising a negative electrode having lithium as a main active material, an organic electrolytic solution, and a positive electrode having bismuth trioxide as a main active material, and a positive electrode pellet after pressure molding having a low density filling. In this case, by granulating the positive electrode mixture, the fluidity of the positive electrode mixture is increased to enable molding by threshing weighing, and by further attaching the binding property to the surface of the granulated particles, a low density filled positive electrode It is intended to provide a positive electrode pellet that is easy to handle by improving the binding property of the pellet to prevent the mixture from falling off or collapsing during transportation or assembly.

〔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ア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 battery, the positive electrode has been manufactured as follows. That is, bismuth trioxide as an active material, a conductive agent such as carbon powder or metal powder such as graphite and carbon black, and a resin binder such as fluororesin and polystyrene are mixed at a predetermined composition ratio, and then this positive electrode mixture is mixed. A predetermined amount of the agent is filled in a mold of a molding machine and pressure-molded together with the positive electrode holding ring to obtain a positive electrode pellet. The positive electrode pellets thus obtained were dried by heating under reduced pressure and sufficiently dehydrated, and then incorporated into a positive electrode can and assembled into a battery. As a method of filling a predetermined amount of the positive electrode mixture in the mold of the molding machine, the mixture is filled in a container (feeder) having a hole for the mixture to drop at the bottom and reciprocated on the mold, or Slippery weighing for moving the mold and filling the mixture in the mold is widely performed.

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。
Further, when a battery of this type is discharged, the volume of the negative electrode lithium decreases as the discharge progresses, and the positive electrode expands. However, since the positive electrode expands more than the volume reduction of the negative electrode lithium, the total thickness of the battery is increased, and in extreme cases, the equipment used is destroyed. Therefore, a method of suppressing the expansion of the positive electrode by filling the positive electrode pellet with a low density is used, and in this case, a positive electrode retaining ring is used for handling during assembly and increasing the strength of the pellet.

〔発明が解決しようとする課題〕[Problems 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, if a predetermined amount of the positive electrode mixture prepared as described above is used,
When filling into the mold of the molding machine by squeeze weighing, the fluidity of the mixture is poor, so the variation in the filling amount is large, and the workability such as weight selection of the positive electrode pellets after pressure molding is reduced.
In addition, there are problems that the positive electrode pellets are chipped or the positive electrode pellets fall off due to uneven filling of the positive electrode mixture, the positive electrode capacity is reduced, and the thickness of the positive electrode pellet is non-uniform and the sealing property is deteriorated.

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 in order to improve the fluidity of the mixture, but when the positive electrode pellets are molded at a low density, the binding property of the positive electrode pellets is weak. There was a problem that the positive electrode pellets collapsed when the granulated particles fell out due to handling or the like, or in the extreme case.

〔課題を解決するための手段〕[Means for Solving the Problems]

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 made various studies, and propose that the positive electrode mixture to which the binder has been added after the positive electrode mixture has been granulated and sized in advance. It is a thing.

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。
That is, the positive electrode mixture is granulated, and the fluidity of the positive electrode mixture is increased by sizing to enable molding by squirrel weighing, and further, a binder adhered to the particle surface, a low density packed positive electrode pellet. It is intended to provide a positive electrode pellet which is easy to handle by enhancing the binding property of the above to suppress the mixture from falling off and collapsing.

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。
If the addition amount of the binder is increased, the fluidity of the positive electrode mixture decreases, so the addition amount is preferably 1.0% or less by weight.

〔作用〕[Action]

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。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。
After mixing and granulating the positive electrode mixture other than the binder in advance 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 added in a dry state. There is little fine powder and the fluidity of particles is high. For this reason, the precision of the crimping measurement is significantly improved. Further, the binding property of the positive electrode pellets is increased because the positive electrode mixture is granulated and then the binding agent dispersed or dissolved in a liquid such as water or an organic solvent is added to the positive electrode pellets to form a powder or the like. It is considered that the binder is sufficiently adhered to the surface of the particles as compared with the case where the particles are added in a dry state, and the binding force between the particles after pellet molding becomes higher. Furthermore, by using the positive electrode retaining 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 described 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
活物質として三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60〜10
0メッシュ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32〜100メッシュの正
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 manufactured as follows. Bismuth trioxide powder and carbon conductive agent (graphite or / and carbon black) as a positive electrode active material were used in a weight ratio.
The mixture was mixed at a ratio of 96: 4, tableted and molded, and then crushed to 60 to 10
The particles were sieved through a 0 mesh sieve. Next, the sizing agent and a binder made of a fluororesin emulsion were mixed in a weight ratio of 99.
Mix at a ratio of 8: 0.2 (net weight of fluororesin), 60 ℃
After being dried for 10 hours, the mixture was passed through a sieve to give a positive electrode mixture (A) of 32 to 100 mesh. The fluororesin emulsion was diluted with 1/10 of the weight of the positive electrode mixture with distilled water so that the net addition amount of the fluororesin was 0.2% by weight. At this time, the yield of the positive electrode mixture (A) was 97%.

又、従来例として、実施例で用いた同じ三酸化ビスマス
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メッシュの正極合剤(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は三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 trioxide powder used in the examples, a carbon conductive agent, and a binder made of a fluororesin emulsion diluted with distilled water were used in a weight ratio of 95.8: 4: 0.2 (net fluororesin weight). After mixing at a ratio of 10 and dried at 60 ° C. for 10 hours, a positive electrode mixture (B) of 32 to 100 mesh was passed through a sieve. At this time, the yield of the positive electrode mixture (B) was 55%. FIG. 1 is a schematic diagram of particles of the positive electrode mixture (A) of the present invention.
In the figure, 1 is a particle made of bismuth trioxide and a carbon conductive agent, and 2 is a binder made of a fluororesin, which is attached to the surface of the particle.

この様にして作製した正極合剤(A、B)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
ペレットを作製した。図において3は正極合剤、4はSU
S製の断面逆L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 positive electrode mixture (A, B) produced in this way, positive electrode pellets having the shape shown in FIG. 2 were produced by molding by squirrel weighing. In the figure, 3 is a positive electrode mixture, 4 is SU
This is a positive electrode holding ring made of S and having an inverted L-shaped cross section. After placing the positive electrode holding ring in an L shape in the mold, a predetermined amount of positive electrode mixture is filled by squirrel weighing and integrally pressure-molded. It was done. Uneven filling of the mixture, dropping of the mixture after molding, and chipping were not seen 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。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。
Table 1 shows the weight measurement results of the positive electrode pellets. The weight is the weight excluding the positive electrode retaining ring, and the measurement quantity is 200 for each.
It is an individual.

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。
As is clear from Table 1, the weight variation of the positive electrode pellet A using the positive electrode mixture (A) of the present invention in which the binder was adhered to the particle surface after the mixture was granulated and sized in advance, , Which is significantly smaller than the positive electrode pellet A using the conventional positive electrode mixture (B). Also, the yield of the positive electrode mixture is remarkably 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で用いたと同じ三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の同様に造粒し、整粒し60〜100メッシュ
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メッシュの正極合剤(C)とした。なお結着剤
の添加は実施例1の同じ方法で行った。又、従来例とし
て、実施例1で用いたと同じ三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。
Example 2 In this example, a positive electrode mixture was manufactured as follows. The same bismuth trioxide powder and carbon conductive agent (graphite or / and carbon black) used in Example 1 were granulated and sized in the same manner as in Example 1 to give particles of 60 to 100 mesh. Next, the weight ratio of this sized mixture to the binder made of the same fluororesin emulsion as used in Example 1 was used.
After mixing in the ratio of 99.4: 0.6, the particles were sized in the same manner as in Example 1.
It was used as a positive electrode mixture (C) of 32 to 100 mesh. The binder was added in the same manner as in Example 1. In addition, as a conventional example, the same bismuth trioxide powder as that used in Example 1, a carbon conductive agent, and a fluororesin emulsion diluted with distilled water were mixed at a weight ratio of 95.4: 4: 0.6 to prepare a conventional example of Example 1. A positive electrode mixture (D) was produced in the same manner as in the example.

この様にして作製した正極合剤(C、D)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C、Dとした。正極ペレッ
トC、Dの重量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 positive electrode mixture (C, D) produced in this manner, a predetermined amount of the positive electrode mixture was filled in the mold by threshing and pressure molding was performed to obtain positive electrode pellets C, D. The results of measuring the weight variation of the positive electrode pellets C and D showed almost the same tendency as in Example 1, and the weight variation of the positive electrode pellet C was extremely small.

〔発明の効果〕〔The invention's effect〕

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
において必要なペレット強度が高く、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 the binder is adhered to the surface of the particles after the mixture is granulated in advance has a small weight variation in molding by squirrel weighing, and assembling, conveying, etc. In the above, the pellet strength required is high, and it has excellent effects such as easy handling.

【図面の簡単な説明】[Brief description 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。 1……正極合剤粒子 2……結着剤 3……正極合剤 4……正極保持リング
FIG. 1 is a schematic view of particles of a positive electrode mixture according to the present invention,
The figure is a cross-sectional view showing an example of a positive electrode pellet according to the present invention. 1 ... Positive electrode mixture particles 2 ... Binder 3 ... Positive electrode mixture 4 ... Positive electrode retaining ring

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】結着剤を含有していない正極活物質と導電
剤からなる正極合剤の粒子の外周表面の一部に高分子結
着剤を付着した正極ペレットを用いたことを特徴とする
有機電解質電池。
1. A positive electrode pellet in which a polymer binder is attached to a part of an outer peripheral surface of a particle of a positive electrode mixture containing a positive electrode active material containing no binder and a conductive agent. Organic electrolyte battery.
【請求項2】正極活物質と導電剤を混合する工程と、 この混合合剤を粒子とする工程と、 この粒子の大きさを所定の粒度範囲に揃える工程と、 この整粒された粒子の外周表面に高分子結着剤を付着す
る工程と、 この外周表面に高分子結着剤を付着した整粒された粒子
を乾燥する工程と、 この乾燥された粒子を所定の粒度範囲に整粒する工程
と、 この整粒された粒子を所定形状に成形する工程と、 この成形された正極ペレットを電池の正極として用いる
工程とからなることを特徴とする有機電解質電池の製造
方法。
2. A step of mixing a positive electrode active material and a conductive agent, a step of forming the mixed mixture into particles, a step of adjusting the size of the particles to a predetermined particle size range, and a step of adjusting the size of the particles. A step of adhering a polymeric binder to the outer peripheral surface; a step of drying the sized particles having a polymeric binder attached to the outer peripheral surface; and a step of sizing the dried particles to a predetermined particle size range. And a step of shaping the sized particles into a predetermined shape, and a step of using the shaped positive electrode pellet as a positive electrode of a battery.
【請求項3】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Bi2O3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おいて、前記正極
として三酸化ビスマスと導電剤等々の結着剤以外の成分
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
して得られる正極合剤を所定形状に成形したものを用い
たことを特徴とする有機電解質電池。
3. An organic electrolyte battery comprising at least a negative electrode containing lithium as a main active material, an organic electrolyte, and a positive electrode containing bismuth trioxide Bi 2 O 3 as a main active material, wherein bismuth trioxide and conductive material are used as the positive electrode. The positive electrode mixture obtained by mixing components other than the binder, such as agents, and granulating in advance, sizing, adding a polymer binder dispersed or dissolved in water or an organic solvent, and drying. An organic electrolyte battery, which is formed into a predetermined shape.
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 JPH02276156A (en) 1990-11-13
JPH0760678B2 true JPH0760678B2 (en) 1995-06-28

Family

ID=14174489

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

Country Status (1)

Country Link
JP (1) JPH0760678B2 (en)

Family Cites Families (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
JPH02276156A (en) 1990-11-13

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