JPH01151158A - Manufacture of positive electrode for nonaqueous solvent cell - Google Patents

Manufacture of positive electrode for nonaqueous solvent cell

Info

Publication number
JPH01151158A
JPH01151158A JP62309714A JP30971487A JPH01151158A JP H01151158 A JPH01151158 A JP H01151158A JP 62309714 A JP62309714 A JP 62309714A JP 30971487 A JP30971487 A JP 30971487A JP H01151158 A JPH01151158 A JP H01151158A
Authority
JP
Japan
Prior art keywords
positive electrode
ptfe
mixture
dispersion
coating
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
JP62309714A
Other languages
Japanese (ja)
Inventor
Masao Ide
井出 正夫
Teruji Yamanobe
山野辺 輝治
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.)
FDK Twicell Co Ltd
Original Assignee
Toshiba Battery 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 Toshiba Battery Co Ltd filed Critical Toshiba Battery Co Ltd
Priority to JP62309714A priority Critical patent/JPH01151158A/en
Publication of JPH01151158A publication Critical patent/JPH01151158A/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
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture

Abstract

PURPOSE:To obtain a positive electrode for a cell excellent in large-current characteristic by kneading, granulating and drying a positive electrode active material, conducting material powder, a thickener and the dispersion of polytetra fluoroethylene(PTFE), coating PTFE on the surface, then forming them into pellets. CONSTITUTION:A positive electrode active material such as MnO, conducting material powder such as graphite, a thickener solution solved with polyacrylic acid or the like in water and polytetra fluoroethylene(PTFE) in water are added and kneaded. The mixture is pressure-extruded into grains, which are dried by a centrifugal granulating machine or the like. The water PTEF dispersion is spray-coated on the surface of the granular black mix. Finally, the coating black mix thus obtained is press-molded into a pellet by a press-molding machine. The positive electrode for a button cell thus produced has the strong binding force among the granular black mix and suppresses the rise of the internal resistance of the cell and shows the excellent large-current characteristic.

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は非水溶媒電池の正極の製造法に関し、さらに詳
しくは、電池性能が優れた非水溶媒電池の正極の製造法
に関する。
[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to a method for manufacturing a positive electrode for a non-aqueous solvent battery, and more specifically, a method for manufacturing a positive electrode for a non-aqueous battery with excellent battery performance. Regarding the law.

(従来の技術および問題点) 現在多く使用されている非水溶媒電池の1例を第1図に
示す。図はボタン型非水溶媒電池の縦断面図である。
(Prior Art and Problems) An example of a non-aqueous solvent battery that is currently widely used is shown in FIG. The figure is a longitudinal cross-sectional view of a button-type non-aqueous solvent battery.

図において、1が正極である。正極lは、MnO2、V
205 、CuO等の活物質を導電材や結着剤等と混練
しペレット化またはシート化したものである。
In the figure, 1 is the positive electrode. The positive electrode l is MnO2, V
205, an active material such as CuO is kneaded with a conductive material, a binder, etc. and formed into pellets or sheets.

2は、負極容器3に圧着された負極で、Li箔またはL
iを主体とするアルカリ金属箔で構成されている。
2 is a negative electrode crimped to the negative electrode container 3, and is made of Li foil or L
It is composed of an alkali metal foil mainly composed of i.

4はセパレータで、例えば多孔質ポリプロビレ。4 is a separator, for example, porous polypropylene.

ン薄膜、ポリプロピレン不織布のような保液性を有する
材料で構成され、正極1の上に載置される。そして、こ
のセパレータ4には、プロピレンカーボネート、1.2
−ジメトキシエタンのような非プロトン性有機溶媒番乙
 L iCI O4+LiA立04  、LiBF4 
 、LiPF6  。
The positive electrode 1 is made of a liquid-retentive material such as a polypropylene thin film or a polypropylene nonwoven fabric, and is placed on the positive electrode 1 . This separator 4 contains propylene carbonate, 1.2
- Aprotic organic solvents such as dimethoxyethane LiCI O4 + LiA 04, LiBF4
, LiPF6.

L i A s F6のような電解質を溶解せしめた所
定濃度の非水電解液が含浸されている。
It is impregnated with a non-aqueous electrolyte of a predetermined concentration in which an electrolyte such as L i As F6 is dissolved.

これら正極l、セパレータ(非水電解液)4、および負
極2は全体として発電要素を構成する。
These positive electrode 1, separator (non-aqueous electrolyte) 4, and negative electrode 2 constitute a power generation element as a whole.

そして、この発電要素が正極容器6および負極容器3か
ら成る電池容器に内蔵されて電池が組立てられる。5は
絶縁バッキングである。
Then, this power generation element is housed in a battery container consisting of a positive electrode container 6 and a negative electrode container 3, and a battery is assembled. 5 is an insulating backing.

このような非水溶媒電池における正極は、例えば、正極
活物質および導電性物質の粉末、増粘剤溶液ならびにポ
リテトラフルオロエチレン(結着剤)のデイスパージョ
ンを混練した後、造粒・乾燥して顆粒状合剤とし、これ
を型に充填し加圧成形してペレット化させる方法により
製造される(特開昭55−93671、特開昭55−9
6557)が、近年電池への大電流放電特性の要求が高
まるにつれ、放電中に正極合剤が膨張して内部抵抗が上
昇し、大電流が取り出せなくなるという問題が生じてき
た。
The positive electrode in such a nonaqueous solvent battery is produced by, for example, kneading a powder of a positive electrode active material and a conductive material, a thickener solution, and a dispersion of polytetrafluoroethylene (binder), followed by granulation and drying. It is produced by a method in which the granular mixture is made into a granular mixture, which is then filled into a mold and pressure-molded to form pellets (JP-A-55-93671, JP-A-55-9).
However, as the demand for large current discharge characteristics for batteries has increased in recent years, a problem has arisen in that the positive electrode mixture expands during discharge, increasing internal resistance and making it impossible to extract large current.

そこで本発明は、内部抵抗が上昇しにくい大電流放電特
性が優れた非水溶媒電池を提供することを目的とする。
Accordingly, an object of the present invention is to provide a non-aqueous solvent battery that is resistant to increases in internal resistance and has excellent large current discharge characteristics.

[発明の構成] (問題点を解決するための手段) 本発明者らは、上述の問題点を解決すべく鋭意検討を重
ねた結果、前記の正極製造の際、顆粒状合剤を加圧成形
する前にポリテトラフルオロエチレン(PTFE)被膜
を形成する工程を加えることにより、目的を達成できる
ことを見出した。
[Structure of the Invention] (Means for Solving the Problems) As a result of intensive studies to solve the above-mentioned problems, the present inventors discovered that the granular mixture was pressurized during the production of the positive electrode. It has been found that the objective can be achieved by adding a step of forming a polytetrafluoroethylene (PTFE) film before molding.

すなわち本発明の非水溶媒電池の正極の製造法は、 (1)正極活物質および導電性物質の粉末、増粘剤溶液
ならびにポリテトラフルオロエチレン(PTFE)のデ
ィスパージョンを混練し、混合物とする工程; (2)
該混合物から造粒し、乾燥して顆粒状合剤とする工程;
 (3)該顆粒状合剤の表面にポリテトラフルオロエチ
レン(PTFE)被膜を形成せしめてコーティング合剤
とする工程; (4)該コーティング合剤を型に充填し
、加圧成形してペレットとする工程;の4工程からなる
ことを特徴とする。
That is, the method for producing a positive electrode for a non-aqueous solvent battery of the present invention is as follows: (1) A mixture is prepared by kneading a positive electrode active material, a conductive material powder, a thickener solution, and a polytetrafluoroethylene (PTFE) dispersion. Process; (2)
A step of granulating the mixture and drying it into a granular mixture;
(3) Forming a polytetrafluoroethylene (PTFE) film on the surface of the granular mixture to obtain a coating mixture; (4) Filling the coating mixture into a mold and press-molding it into pellets. It is characterized by consisting of four steps:

本発明の製造工程について順次説明する。The manufacturing process of the present invention will be sequentially explained.

まず、第1工程において使用される正極活物質としては
、従来の非水溶媒電池において使用されている正極活物
質を使用することができ、例えば、MnO2、V205
 、CuO等が挙げられる。正極活物質は粉末状態で使
用し、好ましくは平均粒径が20戸以下である。
First, as the positive electrode active material used in the first step, positive electrode active materials used in conventional nonaqueous solvent batteries can be used, such as MnO2, V205
, CuO, etc. The positive electrode active material is used in powder form, and preferably has an average particle size of 20 particles or less.

導電性物質としては、例えば黒鉛、アセチレンブラック
、カーボンブラック等の微粉末を使用し、好ましくは比
表面積がlOm′/g以上である。
As the conductive substance, for example, fine powder of graphite, acetylene black, carbon black, etc. is used, and the specific surface area is preferably 1Om'/g or more.

増粘剤溶液としては、例えばポリアクリル酸、ポリアク
リル酸アルカリ金属基、ポリビニルアルコール等を水、
アルコール等の溶媒に、1〜5重量%の濃度で溶解させ
たものである。
As a thickener solution, for example, polyacrylic acid, polyacrylic acid alkali metal group, polyvinyl alcohol, etc. are mixed with water,
It is dissolved in a solvent such as alcohol at a concentration of 1 to 5% by weight.

結着剤として加えるポリテトラフルオロエチレ7 (P
TFE)のディスパージョンは、固形分30〜70重量
%で、水、アルコール等の分散媒に分散させたものであ
る。固形分がこの範囲より少ないと生成物の結着性が悪
く、多すぎるとPTFEが均一に存在しなくなるので好
ましくない。
Polytetrafluoroethylene 7 (P
A dispersion of TFE has a solid content of 30 to 70% by weight and is dispersed in a dispersion medium such as water or alcohol. If the solid content is less than this range, the binding properties of the product will be poor, and if it is too large, the PTFE will not be present uniformly, which is not preferred.

上述のような正極活物質85〜95重量部、導電性物質
5〜15重量部、増粘剤溶液20〜40重量部、PTF
Eディスパージョン1〜5重量部を混合し、攪拌混練し
て粘性を有する湿潤合剤とする。攪拌混線は通常の方法
にて行なうことができる。
85 to 95 parts by weight of positive electrode active material as described above, 5 to 15 parts by weight of conductive material, 20 to 40 parts by weight of thickener solution, PTF
1 to 5 parts by weight of E-dispersion are mixed and stirred and kneaded to obtain a viscous wetting agent. Stirring and cross-mixing can be carried out in a conventional manner.

次に、第1工程で得られた湿潤合剤を造粒し、乾燥して
顆粒状合剤とする第2工程について述べる。造粒は、湿
潤合剤を孔径0.2〜0.8mmの穴より加圧しながら
押し出し、0.5〜1.0)の長さの円柱状の合剤を切
り出すことによって行なう。次いで、これを乾燥するが
、例えば、80〜120°Cの熱乾燥空気を通気させた
遠心造粒機中で、回転数500〜1000rpffi、
0.5〜1時間乾燥させることにより、平均粒径0.2
〜0.8mmの球状の顆粒状合剤とすることができる。
Next, a second step in which the wet mixture obtained in the first step is granulated and dried to form a granular mixture will be described. Granulation is carried out by extruding the wet mixture under pressure through holes with a hole diameter of 0.2 to 0.8 mm, and cutting out a cylindrical mixture with a length of 0.5 to 1.0 mm. Next, this is dried, for example, in a centrifugal granulator through which hot dry air of 80 to 120°C is aerated, at a rotation speed of 500 to 1000 rpm,
By drying for 0.5 to 1 hour, the average particle size is 0.2
It can be made into a spherical granular mixture of ~0.8 mm.

次に、第2工程で得られた顆粒状合剤の表面にPTFE
被膜を形成せしめてコーティング合剤とする第3工程に
ついて述べる。コーティングは、噴霧法、浸漬法等によ
り行なうことができるが、例えば噴霧法の場合には、固
形分30〜70重量%の水性PTFEディスパージョン
を、例えば噴霧コーテイング機等を用いて噴霧する。コ
ーテイング量は、被覆PTFEが顆粒状合剤に対して固
形分として0.2〜1.5重量%となる量である。
Next, PTFE was applied to the surface of the granular mixture obtained in the second step.
The third step of forming a film to obtain a coating mixture will be described. Coating can be carried out by a spraying method, a dipping method, etc. In the case of a spraying method, for example, an aqueous PTFE dispersion having a solid content of 30 to 70% by weight is sprayed using, for example, a spray coating machine. The coating amount is such that the coated PTFE has a solid content of 0.2 to 1.5% by weight based on the granular mixture.

最後に、第3工程で得られたコーティング合剤を型に充
填し、加圧成形してペレットする第4工程について述べ
る。コーティング合剤の目的とする正極の大きさに合わ
せた所定量を成形型に充填し、2〜6tOn/Cff1
2で、例えばプレス成形機等を用いて加圧成形する。
Finally, the fourth step will be described in which the coating mixture obtained in the third step is filled into a mold and pressure-molded into pellets. Fill a mold with a predetermined amount of the coating mixture according to the size of the desired positive electrode, and apply 2 to 6 tOn/Cff1.
In step 2, pressure molding is performed using, for example, a press molding machine.

かくして得られた正極を、第1図に示したような電池に
組み込んで用いた場合には、正極内部において、PTF
Eのコーティングのために顆粒状合剤同志の結着力が強
まり、電池放電中の正極合剤の膨張が抑制され、電解液
が正極合剤中に吸収される割合が減少しリチウム界面ま
たはセパレータ内に保持されるので、内部抵抗の上昇が
抑制されて大電流放電特性が向上する。
When the positive electrode thus obtained is incorporated into a battery as shown in FIG.
Due to the coating of E, the binding force between the granular mixture is strengthened, the expansion of the positive electrode mixture during battery discharge is suppressed, and the rate at which the electrolyte is absorbed into the positive electrode mixture is reduced, resulting in the absorption of the electrolyte at the lithium interface or within the separator. Therefore, an increase in internal resistance is suppressed and large current discharge characteristics are improved.

以下の実施例により本発明をさらに詳しく説明する。The invention will be explained in more detail by the following examples.

(実施例) (1)正極の製造 焼成二酸化マンガン粉末95重量部および黒鉛微粉末(
比表面積20rrf/g)5重量部を混合したもの10
00gに、ポリアクリル酸30gを水300−に溶解さ
せた増粘剤水溶液および固形分60重量%の水性PTF
Eディスパージョン50gを加えた後充分に攪拌混練し
、粘性を有する湿潤合剤を製造した。
(Example) (1) Production of positive electrode 95 parts by weight of calcined manganese dioxide powder and fine graphite powder (
Specific surface area 20rrf/g) mixed with 5 parts by weight10
00 g, a thickener aqueous solution prepared by dissolving 30 g of polyacrylic acid in 300 g of water, and aqueous PTF with a solid content of 60% by weight.
After adding 50 g of E-dispersion, the mixture was sufficiently stirred and kneaded to produce a viscous wetting agent.

次いで、この湿潤合剤を孔径0.5mmの金網より加圧
しながら押し出し、直径0.5mm、長さ0.2〜0.
8mmの円柱状の合剤を切り出した。
Next, this wet mixture was extruded under pressure through a wire mesh with a hole diameter of 0.5 mm, and a diameter of 0.5 mm and a length of 0.2-0.
An 8 mm cylindrical mixture was cut out.

これをloo’cの熱乾燥空気を通気させた遠心造粒機
にて、11000rp、0.5時間処理した後、粒径0
.2〜0.8mmの球状の顆粒状合剤が得られた。
This was processed in a centrifugal granulator with LOOO'C hot dry air at 11,000 rpm for 0.5 hours, and the particle size was 0.
.. A spherical granular mixture with a size of 2 to 0.8 mm was obtained.

さらに、この顆粒状合剤を噴霧コーテイング機にて、固
形分60重量%のPTFEディスパージョンを噴霧コー
ティングしたところ、顆粒状合剤に対し0.3重量%の
PTFEの被膜が形成された。
Furthermore, when this granular mixture was spray-coated with a PTFE dispersion having a solid content of 60% by weight using a spray coating machine, a film of PTFE of 0.3% by weight with respect to the granular mixture was formed.

最後に、このコーティング合剤0.4gをプレス成形機
にて5 ton/Cm2の条件で加圧成形し、直径15
mm厚さ0.65mmのペレットを得、これを正極とし
た。
Finally, 0.4 g of this coating mixture was pressure-molded using a press molding machine under conditions of 5 tons/Cm2, and a diameter of 15
A pellet with a thickness of 0.65 mm was obtained, and this was used as a positive electrode.

(2)電池の組立て ステンレス鋼製の正極容器に、この正極ペレットを着設
し、その上に、ポリプロピレン不織布からなり、プロピ
レンカーボネートと1.2−ジメトキシエタンl:1 
(容量比)の混合溶媒に過塩素酸リチウムを1モル/文
の濃度で溶解した電解液が含浸保持されているセパレー
タを載置し、さらにその上に負極として金属リチウム箔
を載置して、発電要素を構成した。次いでこの上に、ス
テンレス鋼製の負極容器を冠着し、その周縁にポリプロ
ピレンからなる絶縁バッキング(封口体)を介在させ、
正極容器の上方を内側に屈曲して全体をかしめ、第1図
に示したようなボタン型非水溶媒電池を組立てた。
(2) Assembling the battery The positive electrode pellets are placed in a stainless steel positive electrode container, and on top of the positive electrode pellets made of polypropylene nonwoven fabric, propylene carbonate and 1,2-dimethoxyethane are mixed in l:1
A separator impregnated with an electrolytic solution prepared by dissolving lithium perchlorate at a concentration of 1 mole/liter in a mixed solvent of (volume ratio) is placed, and a metal lithium foil is placed on top of it as a negative electrode. , constituted the power generation element. Next, a stainless steel negative electrode container was mounted on top of this, and an insulating backing (sealing body) made of polypropylene was interposed around the periphery.
The upper part of the positive electrode container was bent inward and the whole was caulked to assemble a button type non-aqueous solvent battery as shown in FIG.

(3)連続放電性能試験 かくして製造した本発明による正極を具備した電池につ
いて、20°CにおいてIKΩの負荷抵抗をかけた時の
経時的な端子電圧の降下を測定し、その結果を第2図(
A)に示した。
(3) Continuous discharge performance test Regarding the thus manufactured battery equipped with the positive electrode according to the present invention, the drop in terminal voltage over time when a load resistance of IKΩ was applied at 20°C was measured, and the results are shown in Figure 2. (
Shown in A).

なお、比較例として、上述の正極の製造工程においてP
TFEディスパージョンのコーティングを行なわなかっ
た他は同様にして製造した正極を具備した電池を同様に
して組立て、上述と同一の条件で連続放電性能試験を行
なった結果を(B)として示した。
As a comparative example, P
A battery equipped with a positive electrode manufactured in the same manner except that it was not coated with TFE dispersion was assembled in the same manner, and a continuous discharge performance test was conducted under the same conditions as above. The results are shown as (B).

[発明の効果] 本発明により製造した正極は、顆粒状合剤が加圧成形さ
れる前にPTFEディスパージョンでコーティングされ
ているので、顆粒状合剤同志の結着力が強く、膨張が少
ない。
[Effects of the Invention] Since the positive electrode manufactured according to the present invention is coated with a PTFE dispersion before the granular mixture is pressure-molded, the granular mixture has a strong binding force among itself and has little expansion.

そのため、電池の内部抵抗の上昇が抑制され、大電流放
電特性が優れた寿命の長い電池を提供することができる
Therefore, an increase in internal resistance of the battery is suppressed, and a battery with excellent large current discharge characteristics and long life can be provided.

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

第1図は、ボタン型非水溶媒電池の縦断面図であり、第
2図は、本発明により製造した正極を具備した電池(A
)と従来法により製造した正極を具備した電池(B)の
連続放電性能を比較した図である。
FIG. 1 is a longitudinal cross-sectional view of a button-type nonaqueous solvent battery, and FIG. 2 is a battery (A
) and a battery (B) equipped with a positive electrode manufactured by a conventional method.

Claims (1)

【特許請求の範囲】  正極活物質および導電性物質の粉末、増粘剤溶液なら
びにポリテトラフルオロエチレン(PTFE)のディス
パージョンを混練し、湿潤合剤とする工程;該湿潤合剤
から造粒し、乾燥して顆粒状合剤とする工程;該顆粒状
合剤の表面にポリテトラフルオロエチレン(PTFE)
被膜を形成せしめてコーティング合剤とする工程;該コ
ーティング合剤を型に充填し、加圧成形してペレットと
する工程; からなることを特徴とする非水溶媒電池の正極の製造法
[Claims] A step of kneading a powder of a positive electrode active material and a conductive material, a thickener solution, and a dispersion of polytetrafluoroethylene (PTFE) to form a wetting agent; granulating the wetting agent; , drying to form a granular mixture; polytetrafluoroethylene (PTFE) on the surface of the granular mixture.
1. A method for producing a positive electrode for a non-aqueous battery, comprising the following steps: forming a film to obtain a coating mixture; filling the coating mixture into a mold and press-molding it into pellets;
JP62309714A 1987-12-09 1987-12-09 Manufacture of positive electrode for nonaqueous solvent cell Pending JPH01151158A (en)

Priority Applications (1)

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JP62309714A JPH01151158A (en) 1987-12-09 1987-12-09 Manufacture of positive electrode for nonaqueous solvent cell

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JP62309714A JPH01151158A (en) 1987-12-09 1987-12-09 Manufacture of positive electrode for nonaqueous solvent cell

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JPH01151158A true JPH01151158A (en) 1989-06-13

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1282182A2 (en) 2001-08-02 2003-02-05 Matsushita Electric Industrial Co., Ltd. Positive electrode for non-aqueous electrolyte secondary battery and method of producing the same
KR100471976B1 (en) * 1997-09-23 2005-05-17 삼성에스디아이 주식회사 Electrode mixture granules and preparation method
JP2015220123A (en) * 2014-05-19 2015-12-07 トヨタ自動車株式会社 Nonaqueous electrolyte secondary battery and method for manufacturing the same
JP2018181803A (en) * 2017-04-21 2018-11-15 三洋化成工業株式会社 Manufacturing method of electrode for lithium ion battery

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100471976B1 (en) * 1997-09-23 2005-05-17 삼성에스디아이 주식회사 Electrode mixture granules and preparation method
EP1282182A2 (en) 2001-08-02 2003-02-05 Matsushita Electric Industrial Co., Ltd. Positive electrode for non-aqueous electrolyte secondary battery and method of producing the same
EP1282182A3 (en) * 2001-08-02 2005-04-20 Matsushita Electric Industrial Co., Ltd. Positive electrode for non-aqueous electrolyte secondary battery and method of producing the same
US6942946B2 (en) 2001-08-02 2005-09-13 Matsushita Electric Industrial Co., Ltd. Positive electrode for non-aqueous electrolyte secondary battery and method of producing the same
JP2015220123A (en) * 2014-05-19 2015-12-07 トヨタ自動車株式会社 Nonaqueous electrolyte secondary battery and method for manufacturing the same
JP2018181803A (en) * 2017-04-21 2018-11-15 三洋化成工業株式会社 Manufacturing method of electrode for lithium ion battery

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