JPH076752A - Electrode, method for manufacturing the same, and secondary battery using the electrode - Google Patents

Electrode, method for manufacturing the same, and secondary battery using the electrode

Info

Publication number
JPH076752A
JPH076752A JP5143824A JP14382493A JPH076752A JP H076752 A JPH076752 A JP H076752A JP 5143824 A JP5143824 A JP 5143824A JP 14382493 A JP14382493 A JP 14382493A JP H076752 A JPH076752 A JP H076752A
Authority
JP
Japan
Prior art keywords
electrode
binder
secondary battery
discharge capacity
active material
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
JP5143824A
Other languages
Japanese (ja)
Inventor
Yoshio Matsuda
良夫 松田
Jun Tsukamoto
遵 塚本
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP5143824A priority Critical patent/JPH076752A/en
Publication of JPH076752A publication Critical patent/JPH076752A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)

Abstract

PURPOSE:To increase discharge capacity and cycle life by uniformly dispersing a binder used for an electrode in an electrode material, press molding, and heat treating. CONSTITUTION:To uniformly disperse a binder in an electrode material, an active material, a conductor, and the binder are blended to prepare the electrode material, and the electrode material is placed on a current collector to prepare an electrode and dried. The electrode is press molded to stick the electrode material to the current collector, then heat treated. As the active material, a lithium composite oxide selected from LixCoO2 (0<x<=1.0), LixNiO2 (0<x<=1.0), and LixCoyNi1-yO2 (0<x<=1.0, 0<y<=1.0) is used. The discharge capacity and especially cycle life are increased.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、電極、およびその製造
方法、さらにはその電極を用いた二次電池に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrode, a method for manufacturing the electrode, and a secondary battery using the electrode.

【0002】[0002]

【従来の技術】近年、ビデオカメラやノート型パソコン
などのポータブル機器の普及に伴い、小型高容量の二次
電池に対する需要が高まっている。現在使用されている
二次電池のほとんどはアルカリ電解液を用いたニッケル
−カドミウム電池であるが、電池電圧が約1.2Vと低
く、エネルギー密度の向上は困難である。そのため、負
極にリチウム金属を使用するリチウム二次電池が検討さ
れた。
2. Description of the Related Art In recent years, with the widespread use of portable devices such as video cameras and notebook computers, demand for small and high capacity secondary batteries has increased. Most of the secondary batteries currently used are nickel-cadmium batteries using an alkaline electrolyte, but the battery voltage is low at about 1.2 V, and it is difficult to improve the energy density. Therefore, a lithium secondary battery using lithium metal for the negative electrode has been studied.

【0003】ところが、リチウム金属を負極に使用する
二次電池では、充放電の繰り返しによってリチウムが樹
枝状(デンドライト)に成長し、短絡を起こしたり寿命
が短くなるなどの不都合が生じやすかった。そこで、負
極に各種炭素質材料を用いて、リチウムイオンをドーピ
ング、脱ドーピングすることにより使用する二次電池が
提案された。また、このような各種炭素質材料は、アニ
オンをドーピングして正極として用いることも可能であ
る。上記の炭素質材料へのリチウムイオンあるいはアニ
オンのドーピングを利用した電極を利用した二次電池と
しては、特開昭57−208079号公報、特開昭58
−93176号公報、特開昭58−192266号公
報、特開昭62−90863号公報、特開昭62−12
2066号公報、特開平3−66856号公報等が公知
である。
However, in a secondary battery in which lithium metal is used as the negative electrode, lithium tends to grow into dendrites due to repeated charging / discharging, resulting in short circuits and shortened life. Therefore, there has been proposed a secondary battery in which various carbonaceous materials are used for the negative electrode and used by doping and dedoping with lithium ions. Further, such various carbonaceous materials can be used as a positive electrode after being doped with anions. Secondary batteries using electrodes made by doping lithium ions or anions into the above carbonaceous materials are disclosed in JP-A-57-208079 and JP-A-58.
-93176, JP-A-58-192266, JP-A-62-90863, and JP-A-62-12.
Japanese Laid-Open Patent Publication No. 2066 and Japanese Laid-Open Patent Publication No. 3-66856 are known.

【0004】このような炭素質材料としては、粉末の形
状のもの、炭素繊維あるいは炭素繊維構造体など、いず
れの形態で用いてもよい。
Such carbonaceous material may be used in any form such as powder, carbon fiber or carbon fiber structure.

【0005】さらに、最近では、高エネルギー密度化の
要求に応えるべく、電池電圧が4V前後を示すものが現
れ、注目を浴びている。電池電圧の高電圧化は、正極に
高電位を示す活物質の探索、開発によって進められ、ア
ルカリ金属を含む遷移金属酸化物や遷移金属カルコゲン
などの無機化合物が知られている。なかでも、Lix
oO2 (0<x≦1.0)、Lix NiO2 (0<x≦
1.0)およびLixCoy Ni1-y 2 (0<x≦
1.0、0<y≦1.0)などが、高電位、安定性、長
寿命という点から最も有望である。
Further, recently, in order to meet the demand for higher energy density, a battery voltage of around 4V has appeared and has attracted attention. Higher battery voltage has been pursued by searching for and developing an active material exhibiting a high potential in the positive electrode, and inorganic compounds such as transition metal oxides and transition metal chalcogens containing alkali metals are known. Among them, Li x C
oO 2 (0 <x ≦ 1.0), Lix NiO 2 (0 <x ≦
1.0) and Li x Co y Ni 1-y O 2 (0 <x ≦
1.0, 0 <y ≦ 1.0) and the like are the most promising in terms of high potential, stability, and long life.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、これら
のリチウム複合酸化物を正極活物質に用いた場合でも、
充放電サイクルを繰り返すことにより、放電容量の劣化
(減少)が認められ、数100回の充放電を繰り返すこ
とが要求される二次電池として実用上の問題である。
However, even when these lithium composite oxides are used for the positive electrode active material,
By repeating the charge / discharge cycle, deterioration (reduction) of the discharge capacity is recognized, and this is a practical problem as a secondary battery in which charge / discharge is required to be repeated several hundred times.

【0007】[0007]

【課題を解決するための手段】本発明は、上記課題を解
決するために以下の構成を有するものである。
The present invention has the following constitution in order to solve the above problems.

【0008】「(1) 電池電極を構成する結着剤が、電極
材中に均一に分散していることを特徴とする電極。
"(1) An electrode characterized in that a binder constituting a battery electrode is uniformly dispersed in an electrode material.

【0009】(2) (1)電極活物質、導電剤、結着剤を
混合して電極材を作製する工程、(2)上記電極材を集
電体上に形成して電極を作製する工程、(3)上記電極
を乾燥させる工程、(4)上記電極を加圧成形し、電極
材を集電体に密着させる工程、(5)上記の電極を熱処
理する工程、からなることを特徴とする上記1記載の電
極の製造方法。
(2) (1) A step of preparing an electrode material by mixing an electrode active material, a conductive agent and a binder, and (2) a step of forming the electrode material on a current collector to prepare an electrode. , (3) a step of drying the electrode, (4) a step of press-molding the electrode and bringing an electrode material into close contact with a current collector, and (5) a step of heat-treating the electrode. 2. The method for producing the electrode according to 1 above.

【0010】(3) 上記(1) 記載の電極を用いることを特
徴とする二次電池。」本発明の電極は、一次電池、二次
電池、燃料電池など、どのような電池に利用されるかは
特に限定されるものではない。この中で、二次電池の正
極あるいは負極に好ましく用いられる。特に好ましい二
次電池としては、上述のようにアルカリ金属塩を含む非
水電解液を用いた二次電池を挙げることができる。そこ
で、以下、リチウム二次電池を例に取り挙げ、具体例を
挙げながら詳述する。
(3) A secondary battery using the electrode described in (1) above. The electrode of the present invention is not particularly limited in what kind of battery such as a primary battery, a secondary battery and a fuel cell is used. Among them, it is preferably used as a positive electrode or a negative electrode of a secondary battery. As a particularly preferable secondary battery, a secondary battery using a non-aqueous electrolytic solution containing an alkali metal salt as described above can be mentioned. Therefore, a lithium secondary battery will be taken as an example and described in detail below with specific examples.

【0011】本発明者らは、充放電サイクルによるリチ
ウム二次電池の放電容量の劣化の原因について鋭意検討
した結果、電極材中の結着剤の分布が放電容量の劣化に
大きく影響していることを見い出した。すなわち、リチ
ウム二次電池の場合、ポリフッ化ビニリデン(PVD
F)やポリテトラフッ化エチレンなどのフッ素系樹脂を
結着剤に用いることが多く、通常、N−メチルピロドリ
ンなどの有機溶剤に溶かして、スラリー状にして集電体
に、例えば、バーコーターやドクターナイフなどによっ
て、均一の厚さに塗布している。しかしながら、混合が
不十分であったり、乾燥中に分離してしまうなどの要因
によって、乾燥後の電極剤中の結着剤は、必ずしも均一
に分散していない。ここでいう均一とは、SEMによる
形態観察で、電極の表面および断面において、結着剤
が,少なくとも電極活物質や導電剤の粒子径よりも大き
く偏在した部分がなく、および/または、5〜10個程
度以上の電極活物質や導電剤粒子が結着剤に接触してい
ない部分がない状態をいう。結着剤の偏在による過電圧
によって、放電容量が小さくなったり、結着剤の不足に
よる結着力の不十分さによって、充放電サイクルにとも
なって放電容量の劣化を引き起こしてしまう問題があっ
た。
The inventors of the present invention have made extensive studies on the cause of the deterioration of the discharge capacity of the lithium secondary battery due to the charge / discharge cycle. As a result, the distribution of the binder in the electrode material has a great influence on the deterioration of the discharge capacity. I found a thing. That is, in the case of a lithium secondary battery, polyvinylidene fluoride (PVD
Fluorine-based resins such as F) and polytetrafluoroethylene are often used as a binder, and are usually dissolved in an organic solvent such as N-methylpyrrodoline to form a slurry for a current collector, such as a bar coater or It is applied to a uniform thickness with a doctor knife. However, due to factors such as insufficient mixing and separation during drying, the binder in the dried electrode agent is not always uniformly dispersed. The term "uniform" as used herein means morphological observation by SEM, and there is no portion where the binder is unevenly distributed at least larger than the particle size of the electrode active material or the conductive agent on the surface and cross section of the electrode, and / or 5 to It refers to a state in which there is no portion where about 10 or more electrode active materials or conductive agent particles are not in contact with the binder. There are problems that the discharge capacity is reduced due to overvoltage due to uneven distribution of the binder, and the discharge capacity is deteriorated with charge / discharge cycles due to insufficient binding force due to insufficient binder.

【0012】本発明者らは、かかる問題を解決すべく、
さらに検討した結果、一軸プレスやローラープレスによ
って加圧成形後、熱処理することによって、均一に結着
剤が分散した電極を得られることを見い出した。これ
は、加圧後熱処理することによって、結着剤が電極活物
質、導電剤、集電体に均一になじむからであると考えて
いる。熱処理温度は結着剤が流動性を持つような温度以
上であればよく、好ましくは、結着剤の融点以上の温度
であり、さらに好ましくは、融点よりも20〜50℃高
い温度である。熱処理温度が低すぎると効果的な流動性
が得られにくく、また、高すぎると結着剤に用いる樹脂
が変質・劣化してしまったり、結着剤が集電体と電極材
の界面に溜まってしまうおそれある。さらに、熱処理時
間も上述の熱処理温度と同様の理由で、好適な時間があ
る。例えば、上述のPVDFの場合、融点が180℃程
度のもののでは、200〜220℃で、10〜20分が
好適である。熱処理温度と熱処理温度は、熱処理温度が
高いほど熱処理時間は短くなる傾向にある。
[0012] The inventors of the present invention, in order to solve such a problem,
As a result of further study, it was found that an electrode in which the binder is uniformly dispersed can be obtained by pressure-forming with a uniaxial press or roller press and then heat-treating. It is considered that this is because the binder is uniformly blended with the electrode active material, the conductive agent and the current collector by heat treatment after pressurization. The heat treatment temperature may be higher than the temperature at which the binder has fluidity, preferably the melting point of the binder or higher, and more preferably 20 to 50 ° C. higher than the melting point. If the heat treatment temperature is too low, it is difficult to obtain effective fluidity, and if it is too high, the resin used as the binder may deteriorate or deteriorate, or the binder may accumulate at the interface between the current collector and the electrode material. There is a risk that Further, the heat treatment time is also suitable for the same reason as the heat treatment temperature described above. For example, in the case of PVDF described above, if the melting point is about 180 ° C., 200 to 220 ° C. and 10 to 20 minutes are preferable. Regarding the heat treatment temperature and the heat treatment temperature, the higher the heat treatment temperature, the shorter the heat treatment time tends to be.

【0013】すなわち、上述の電極製造方法をまとめれ
ば、以下のようになる。
That is, the electrode manufacturing method described above is summarized as follows.

【0014】(1)電極活物質、導電剤、結着剤を混合
して電極材を作製する工程。 (2)上記電極材を集電体上に形成して電極を作製する
工程。
(1) A step of preparing an electrode material by mixing an electrode active material, a conductive agent and a binder. (2) A step of forming an electrode by forming the electrode material on a current collector.

【0015】(3)上記電極を乾燥させる工程。(3) A step of drying the electrode.

【0016】(4)上記電極を加圧成形し、電極材を集
電体に密着させる工程。
(4) A step of pressure-molding the above electrode and bringing the electrode material into close contact with the current collector.

【0017】(5)上記の電極を熱処理して結着剤を電
極活物質、導電剤、集電体に均一になじませて、結着力
を増す工程。
(5) A step of increasing the binding force by heat-treating the above-mentioned electrode to uniformly apply the binding agent to the electrode active material, the conductive agent and the current collector.

【0018】本発明に用いられる正極としては、アルカ
リ金属を含む遷移金属酸化物や遷移金属カルコゲンなど
の無機化合物、ポリアセチレン、ポリパラフェニレン、
ポリフェニレンビニレン、ポリアニリン、ポリピロー
ル、ポリチオフェンなどの共役系高分子、ジスルフィド
結合を有する架橋高分子、塩化チオニルなど、通常の二
次電池において用いられる正極を挙げることができる。
これらの中で、リチウム塩を含む非水電解液を用いた二
次電池の場合には、コバルト、マンガン、モリブデン、
バナジウム、クロム、鉄、銅、チタンなどの遷移金属酸
化物や遷移金属カルコゲンが好ましく用いられる。特に
前述のように、Lix CoO2 (0<x≦1.0)、L
x NiO2 (0<x≦1.0)およびLix Coy
1-y 2(0<x≦1.0、0<y≦1.0)など
が、高電位、安定性、長寿命という点から最も有望であ
る。
The positive electrode used in the present invention includes inorganic compounds such as transition metal oxides and transition metal chalcogens containing an alkali metal, polyacetylene, polyparaphenylene,
Examples of the positive electrode used in ordinary secondary batteries include conjugated polymers such as polyphenylene vinylene, polyaniline, polypyrrole, and polythiophene, crosslinked polymers having a disulfide bond, and thionyl chloride.
Among these, in the case of a secondary battery using a non-aqueous electrolyte containing a lithium salt, cobalt, manganese, molybdenum,
Transition metal oxides and transition metal chalcogens such as vanadium, chromium, iron, copper and titanium are preferably used. In particular, as described above, Li x CoO 2 (0 <x ≦ 1.0), L
i x NiO 2 (0 <x ≦ 1.0) and Li x Co y N
i 1 -y O 2 (0 <x ≦ 1.0, 0 <y ≦ 1.0) and the like are the most promising from the viewpoint of high potential, stability, and long life.

【0019】本発明に用いられる炭素質材料としては、
特に限定されるものではなく、一般に有機物を焼成した
ものが用いられる。炭素質材料の電子伝導性が集電の目
的に対して充分に高い場合は、導電剤を添加する必要は
ない。炭素繊維の場合も同様であり、具体的には、ポリ
アクリロニトリル(PAN)から得られるPAN系炭素
繊維、石炭もしくは石油などのピッチから得られるピッ
チ系炭素繊維、セルロースから得られるセルロース系炭
素繊維、低分子量有機物の気体から得られる気相成長炭
素繊維などが挙げられるが、そのほかに、ポリビニルア
ルコール、リグニン、ポリ塩化ビニル、ポリアミド、ポ
リイミド、フェノール樹脂、フルフリルアルコールなど
を焼成して得られる炭素繊維でも構わない。これらの炭
素繊維の中で、炭素繊維が用いられる電極および電池の
特性に応じて、その特性を満たす炭素繊維が適宜選択さ
れることが必要となる。
The carbonaceous material used in the present invention includes:
The material is not particularly limited, and a material obtained by firing an organic material is generally used. When the electron conductivity of the carbonaceous material is sufficiently high for the purpose of collecting electricity, it is not necessary to add a conductive agent. The same applies to the case of carbon fiber, specifically, PAN-based carbon fiber obtained from polyacrylonitrile (PAN), pitch-based carbon fiber obtained from pitch of coal or petroleum, cellulose-based carbon fiber obtained from cellulose, Examples thereof include vapor grown carbon fibers obtained from a gas of a low molecular weight organic substance. In addition, carbon fibers obtained by firing polyvinyl alcohol, lignin, polyvinyl chloride, polyamide, polyimide, phenol resin, furfuryl alcohol, etc. But it doesn't matter. Among these carbon fibers, depending on the characteristics of the electrode and battery in which the carbon fibers are used, it is necessary to appropriately select the carbon fibers that satisfy the characteristics.

【0020】上記炭素繊維の中で、アルカリ金属塩を含
む非水電解液を用いた二次電池の負極に使用する場合に
は、PAN系炭素繊維、ピッチ系炭素繊維、気相成長炭
素繊維が好ましい。特に、アルカリ金属イオン、特にリ
チウムイオンのドーピングが良好であるという点で、P
AN系炭素繊維やピッチ系炭素繊維が好ましく、この中
でも、東レ(株)製の”トレカ”Tシリーズ、また
は、”トレカ”MシリーズなどのPAN系炭素繊維、メ
ゾフェーズピッチコークスを焼成して得られるピッチ系
炭素繊維がさらに好ましく用いられる。
Among the above carbon fibers, when used as a negative electrode of a secondary battery using a non-aqueous electrolyte containing an alkali metal salt, PAN-based carbon fibers, pitch-based carbon fibers and vapor-grown carbon fibers are preferable. In particular, in terms of good doping with alkali metal ions, especially lithium ions, P
AN-based carbon fibers and pitch-based carbon fibers are preferable, and among them, PAN-based carbon fibers such as "Torayca" T series or "Torayca" M series manufactured by Toray Industries, Inc. and mesophase pitch coke are obtained by firing. Pitch-based carbon fibers are more preferably used.

【0021】炭素繊維を電極にする際には、どのような
形態をとっても構わないが、一軸方向に配置したり、も
しくは布帛状やフェルト状の構造体にするなどが、好ま
しい形態となる。布帛状あるいはフェルト状などの構造
体としては、織物、編物、組物、レース、網、フェル
ト、紙、不織布、マットなどが挙げられるが、炭素繊維
の性質や電極特性などの点から、織物やフェルトなどが
好ましい。
When the carbon fiber is used as an electrode, it may have any form, but a preferred form is to arrange it in a uniaxial direction, or to form a fabric-like or felt-like structure. Examples of the fabric-like or felt-like structure include woven fabrics, knitted fabrics, braids, laces, nets, felts, papers, non-woven fabrics, mats, and the like. Felt and the like are preferred.

【0022】本発明の電極を用いた二次電池の電解液と
しては、特に限定されることなく従来の電解液が用いら
れ、例えば酸あるいはアルカリ水溶液、または非水溶媒
などが挙げられる。この中で、上述のアルカリ金属塩を
含む非水電解液からなる二次電池の電解液としては、プ
ロピレンカーボネート、エチレンカーボネート、γ-ブ
チロラクトン、N- メチルピロリドン、アセトニトリ
ル、N,N−ジメチルホルムアミド、ジメチルスルフォ
キシド、テトラヒドロフラン、1,3−ジオキソラン、
ギ酸メチル、スルホラン、オキサゾリドン、塩化チオニ
ル、1,2−ジメトキシエタン、ジエチレンカーボネー
トや、これらの誘導体や混合物などが好ましく用いられ
る。電解液に含まれる電解質としては、アルカリ金属、
特にリチウムのハロゲン化物、過塩素酸塩、チオシアン
塩、ホウフッ化塩、リンフッ化塩、砒素フッ化塩、アル
ミニウムフッ化塩、トリフルオロメチル硫酸塩などが好
ましく用いられる。
The electrolytic solution of the secondary battery using the electrode of the present invention is not particularly limited, and a conventional electrolytic solution may be used, and examples thereof include an acid or alkaline aqueous solution or a non-aqueous solvent. Among these, as the electrolytic solution of the secondary battery composed of the above-mentioned non-aqueous electrolytic solution containing an alkali metal salt, propylene carbonate, ethylene carbonate, γ-butyrolactone, N-methylpyrrolidone, acetonitrile, N, N-dimethylformamide, Dimethyl sulfoxide, tetrahydrofuran, 1,3-dioxolane,
Methyl formate, sulfolane, oxazolidone, thionyl chloride, 1,2-dimethoxyethane, diethylene carbonate, derivatives and mixtures of these are preferably used. The electrolyte contained in the electrolytic solution is an alkali metal,
Particularly, lithium halides, perchlorates, thiocyanates, borofluorides, phosphorous fluorides, arsenic fluorides, aluminum fluorides, trifluoromethylsulfates and the like are preferably used.

【0023】本発明の電極を用いた二次電池の用途とし
ては、軽量かつ高容量で高エネルギー密度の特徴を利用
して、ビデオカメラ、パソコン、ワープロ、ラジカセ、
携帯電話などの携帯用小型電子機器に広く利用可能であ
る。
The secondary battery using the electrode of the present invention can be used as a video camera, a personal computer, a word processor, a radio-cassette, by utilizing the features of light weight, high capacity and high energy density.
It is widely applicable to portable small electronic devices such as mobile phones.

【0024】[0024]

【実施例】本発明の具体的実施態様を以下に実施例をも
って述べるが、本発明はこれに限定されるものではな
い。
EXAMPLES Specific embodiments of the present invention will be described below with reference to examples, but the present invention is not limited thereto.

【0025】実施例1 市販の炭酸リチウム(Li2 CO3 )と塩基性炭酸コバ
ルト(2CoCO2 ・3Co(OH)2 をモル比でLi
/Co=1/1となるように秤量、ジルコニア製ボール
ミルで湿式混合(粉砕溶媒にエタノール使用)後、90
0℃で20時間熱処理してLiCoO2 を合成した。こ
れを上記ボールミルで粉砕してLiCoO2 粉末を得
た。この粉末に導電剤として人工黒鉛を、結着剤として
ポリフッ化ビニリデン(以下PVDFと略称する)をそ
れぞれ10重量部、3重量部添加し、溶媒で粘度調整し
てペースト状にした。これを、予め#1000のエメリ
ー紙で擦り表面を粗しておいた厚さ20μmのアルミ箔
上に塗布し、乾燥後、ローラープレスし、さらに200
℃で15分間熱処理して、電極部の幅10mm,長さ2
0mmのLiCoO2 電極を作製した。同様にして作製
した電極について、SEMによる形態観察を行ったとこ
ろ、電極の表面および断面において、結着剤が、LiC
oO2 や人工黒鉛の粒子径よりも大きく偏在した部分が
なく、かつ、8個以上のLiCoO2 や人工黒鉛粒子が
結着剤に接触していない部分がなかった。
Example 1 Commercially available lithium carbonate (Li 2 CO 3 ) and basic cobalt carbonate (2CoCO 2 .3Co (OH) 2 were used in a molar ratio of Li.
/ Co = 1/1, weighed with a zirconia ball mill (we use ethanol as a grinding solvent), and then 90
LiCoO 2 was synthesized by heat treatment at 0 ° C. for 20 hours. This was crushed with the above ball mill to obtain LiCoO 2 powder. Artificial graphite was added to this powder as a conductive agent, and 10 parts by weight and 3 parts by weight of polyvinylidene fluoride (hereinafter abbreviated as PVDF) as a binder were added, and the viscosity was adjusted with a solvent to form a paste. This is applied to an aluminum foil having a thickness of 20 μm whose surface has been rubbed with # 1000 emery paper beforehand, dried, and roller-pressed, and further 200
Heat treatment for 15 minutes at ℃, width of electrode part 10mm, length 2
A 0 mm LiCoO 2 electrode was prepared. Morphological observation by an SEM was performed on the electrode prepared in the same manner. As a result, it was found that the binder was LiC on the surface and cross section of the electrode.
There was no part that was unevenly distributed larger than the particle size of oO 2 or artificial graphite, and there was no part where 8 or more LiCoO 2 or artificial graphite particles were not in contact with the binder.

【0026】次に、電極の放電容量の評価を行った。電
解液は1MLiPF6 を含むプロピレンカーボネート、
対極および参照極には金属リチウム箔を用いる、3極式
セルで評価した。LiCoO2 当たりの電流密度は50
mA/gの定電流で、4.3V(vs.Li+ /Li)まで充電し
た。この時の充電量は156mAh/gであった。充電
後に、充電と同じ電流密度で3.0V(vs.Li+ /Li)まで
放電した電荷量から求められるLiCoO2 電極の放電
容量は、150mAh/gであった。さらに、充放電サ
イクルを繰り返し、50回目の放電容量と1回目の放電
容量を比較したところ、次式で表される放電容量保持率
は92%であった。
Next, the discharge capacity of the electrode was evaluated. The electrolyte is propylene carbonate containing 1M LiPF 6 ,
Evaluation was carried out using a three-electrode cell in which metallic lithium foil was used for the counter electrode and the reference electrode. The current density per LiCoO 2 is 50
It was charged to 4.3 V (vs. Li + / Li) at a constant current of mA / g. The charge amount at this time was 156 mAh / g. After charging, the discharge capacity of the LiCoO 2 electrode was 150 mAh / g, which was calculated from the amount of charge discharged to 3.0 V (vs. Li + / Li) at the same current density as charging. Further, when the charge and discharge cycle was repeated and the 50th discharge capacity and the 1st discharge capacity were compared, the discharge capacity retention rate represented by the following equation was 92%.

【0027】放電容量保持率(%)=(50回目の放電
容量/1回目の放電容量)×100 比較例1 電極の熱処理を行わないこと以外は、実施例1と同じL
iCoO2 を用いて、実施例1と同様に電極を作製し、
充放電評価を行った。この時の充電量は154mAh/
g、放電容量は、148mAh/gであったが、放電容
量保持率は、82%であった。また、実施例1と同様に
して、SEMによる電極の形態観察を行ったところ、電
極の表面において、結着剤が、LiCoO2 や人工黒鉛
の粒子径よりも大きく偏在した部分があり、かつ、少な
くとも15個以上のLiCoO2や人工黒鉛粒子が結着
剤に接触していない部分があった。
Discharge capacity retention rate (%) = (50th discharge capacity / first discharge capacity) × 100 Comparative Example 1 Same as Example 1 except that heat treatment of the electrode was not performed.
An electrode was prepared in the same manner as in Example 1 using iCoO 2 ,
Charge / discharge evaluation was performed. The charging amount at this time is 154 mAh /
g, the discharge capacity was 148 mAh / g, but the discharge capacity retention rate was 82%. Further, when the morphology of the electrode was observed by SEM in the same manner as in Example 1, there was a portion on the surface of the electrode in which the binder was unevenly distributed larger than the particle diameters of LiCoO 2 and artificial graphite, and There was a portion where at least 15 or more of LiCoO 2 and artificial graphite particles were not in contact with the binder.

【0028】実施例2 塩基性炭酸コバルトの代わりに、塩基性炭酸ニッケル
(NiCO3 ・2Ni(OH)2 ・4H2 O)を用いた
ほかは、実施例1と同様にしてLiNiO2 電極を作製
し、充電電位を4.2V(vs.Li+ /Li)とした以外は、実
施例1と同様に充放電評価を行った。この時の充電量は
147mAh/g、放電容量は、144mAh/gで、
放電容量保持率は、91%であった。また、実施例1と
同様にして、SEMによる電極の形態観察を行ったとこ
ろ、電極の表面および断面において、結着剤が、LiN
iO2 や人工黒鉛の粒子径よりも大きく偏在した部分が
なく、かつ、10個以上のLiNiO2 や人工黒鉛粒子
が結着剤に接触していない部分がなかった。
Example 2 A LiNiO 2 electrode was prepared in the same manner as in Example 1 except that basic nickel carbonate (NiCO 3 .2Ni (OH) 2 .4H 2 O) was used instead of basic cobalt carbonate. Then, charge and discharge evaluation was performed in the same manner as in Example 1 except that the charge potential was 4.2 V (vs. Li + / Li). At this time, the charge amount was 147 mAh / g, the discharge capacity was 144 mAh / g,
The discharge capacity retention rate was 91%. Further, when the morphology of the electrode was observed by the SEM in the same manner as in Example 1, it was found that the binder was LiN on the surface and cross section of the electrode.
There was no portion that was unevenly distributed larger than the particle size of iO 2 or artificial graphite, and there was no portion where 10 or more LiNiO 2 or artificial graphite particles were not in contact with the binder.

【0029】比較例2 熱処理を行わないこと以外は、実施例2と同じLiNi
2 を用いて、実施例2と同様に電極を作製し、充放電
評価を行った。この時の充電量は145mAh/g、放
電容量は、142mAh/gであったが、放電容量保持
率は、78%であった。また、比較例1と同様にして、
SEMによる電極の形態観察を行ったところ、電極の表
面において、結着剤が、LiNiO2 や人工黒鉛の粒子
径よりも大きく偏在した部分があり、かつ、少なくとも
20個以上のLiNiO2 や人工黒鉛粒子が結着剤に接
触していない部分があった。
Comparative Example 2 The same LiNi as in Example 2 except that no heat treatment was performed.
An electrode was prepared using O 2 in the same manner as in Example 2, and charge / discharge evaluation was performed. At this time, the charge amount was 145 mAh / g and the discharge capacity was 142 mAh / g, but the discharge capacity retention rate was 78%. Also, in the same manner as in Comparative Example 1,
When the morphology of the electrode was observed by SEM, the surface of the electrode had a portion where the binder was unevenly distributed larger than the particle diameters of LiNiO 2 and artificial graphite, and at least 20 or more of LiNiO 2 and artificial graphite were found. There were parts where the particles did not come into contact with the binder.

【0030】実施例3 実施例1および実施例2で用いた電極活物質原料を用い
て、酸化物換算でLi1.0 (Co0.5 Ni0.5 )O2
なるように、秤量、混合後、実施例2と同様にして電極
を作製し、同様の熱処理を行った。実施例1と同様に充
放電評価を行った。この時の充電量は156mAh/g
で、放電容量は、149mAh/gで、放電容量保持率
は、92%であった。また、実施例1と同様にして、S
EMによる電極の形態観察を行ったところ、電極の表面
および断面において、結着剤が,Li1.0 (Co0.5
0.5 )O2 や人工黒鉛の粒子径よりも大きく偏在した
部分がなく、かつ、8個以上のLi1.0 (Co0.5 Ni
0.5 )O2 や人工黒鉛が結着剤に接触していない部分が
なかった。
Example 3 The electrode active material raw materials used in Examples 1 and 2 were weighed and mixed to obtain Li 1.0 (Co 0.5 Ni 0.5 ) O 2 in terms of oxide. An electrode was prepared in the same manner as in 2, and the same heat treatment was performed. Charge / discharge evaluation was performed in the same manner as in Example 1. The charging amount at this time is 156 mAh / g
The discharge capacity was 149 mAh / g, and the discharge capacity retention rate was 92%. Further, as in the first embodiment, S
When the morphology of the electrode was observed by EM, it was found that the binder was Li 1.0 (Co 0.5 N
i 0.5 ) O 2 and there is no portion unevenly distributed larger than the particle size of artificial graphite, and eight or more Li 1.0 (Co 0.5 Ni)
0.5 ) There was no part where O 2 or artificial graphite did not come into contact with the binder.

【0031】比較例3 熱処理を行わないこと以外は、実施例3と同じLi1.0
(Co0.5 Ni0.5 )O2 を用いて、実施例3と同様に
電極を作製し、充放電評価を行った。この時の充電量は
148mAh/gで、放電容量は、144mAh/gで
あったが、放電容量保持率は、79%であった。また、
比較例1と同様にして、SEMによる電極の形態観察を
行ったところ、電極の表面において、結着剤が、Li
1.0 (Co0.5 Ni0.5 )O2 や人工黒鉛の粒子径より
も大きく偏在した部分があり、かつ、少なくとも15個
以上のLi1.0 (Co0.5 Ni0.5 )O2 や人工黒鉛粒
子が結着剤に接触していない部分があった。
Comparative Example 3 Li 1.0 as in Example 3 except that no heat treatment was performed.
An electrode was prepared in the same manner as in Example 3 using (Co 0.5 Ni 0.5 ) O 2 , and the charge and discharge was evaluated. At this time, the charge amount was 148 mAh / g and the discharge capacity was 144 mAh / g, but the discharge capacity retention rate was 79%. Also,
When the morphology of the electrode was observed by SEM in the same manner as in Comparative Example 1, it was found that the binder was Li
1.0 (Co 0.5 Ni 0.5 ) O 2 or artificial graphite has a portion unevenly distributed larger than the particle diameter, and at least 15 or more Li 1.0 (Co 0.5 Ni 0.5 ) O 2 or artificial graphite particles are used as the binder. There was a part that was not in contact.

【0032】実施例4 市販のピッチコークスと、結着剤としてPVDFをそれ
ぞれ90重量部、10重量部添加し、溶媒で粘度調整し
てペースト状にした。これを、予め#1000のエメリ
ー紙で擦り表面を粗にしておいた厚さ20μmの銅箔上
に塗布し、乾燥後、ローラープレスし、さらに200℃
で15分間熱処理して、電極部の幅10mm,長さ20
mmの電極を作製した。
Example 4 90 parts by weight and 10 parts by weight of commercially available pitch coke and PVDF as a binder were added, and the viscosity was adjusted with a solvent to form a paste. This is applied to a copper foil having a thickness of 20 μm whose surface has been rubbed with # 1000 emery paper in advance, dried, and roller-pressed, and further 200 ° C.
Heat treatment for 15 minutes at a width of 10 mm and a length of 20
A mm electrode was prepared.

【0033】次に、このようにして作製した電極の放電
容量の評価を行った。電解液は1MLiPF6 を含むプ
ロピレンカーボネート、対極および参照極には金属リチ
ウム箔を用いる、3極式セルで評価した。ピッチコーク
ス当たりの電流密度は40mA/gの定電流で、0.0
V(vs.Li+ /Li)まで充電した。この時の充電量は300
mAh/gであった。充電後に、充電と同じ電流密度で
1.5V(vs.Li+ /Li)まで放電した電荷量から求められ
る電極の放電容量は、220mAh/gで、放電容量保
持率は88%であった。また、実施例1と同様にして、
SEMによる電極の形態観察を行ったところ、電極の表
面および断面において、結着剤が,ピッチコークスの粒
子径よりも大きく偏在した部分がなく、かつ、5個以上
のピッチコークス粒子が結着剤に接触していない部分が
なかった。
Next, the discharge capacity of the electrode thus manufactured was evaluated. The electrolytic solution was evaluated by a three-electrode type cell using propylene carbonate containing 1M LiPF 6 and metallic lithium foil for the counter electrode and the reference electrode. The current density per pitch coke is 0.0 mA at a constant current of 40 mA / g.
It was charged to V (vs. Li + / Li). The charge amount at this time is 300
It was mAh / g. After charging, the discharge capacity of the electrode was 220 mAh / g, which was calculated from the amount of charge discharged to 1.5 V (vs. Li + / Li) at the same current density as charging, and the discharge capacity retention rate was 88%. Also, in the same manner as in Example 1,
When the electrode morphology was observed by SEM, there was no portion where the binder was unevenly distributed over the pitch coke particle size on the surface and cross section of the electrode, and 5 or more pitch coke particles were formed as the binder. There was no part that was not in contact with.

【0034】比較例4 熱処理を行わないこと以外は、実施例4と同様にしてピ
ッチコークス電極を作製した。実施例4と同様に電極の
充放電評価を行った。充電後、40mA/gの定電流で
放電させた時の放電容量は、ピッチコークスの重量当た
りで210mAh/gであったが、放電容量保持率は、
72%であった。また、比較例1と同様にして、SEM
による電極の形態観察を行ったところ、電極の表面およ
び断面において、10個以上のピッチコークス粒子が結
着剤に接触していない部分はなかったが、電極の表面に
おいて、結着剤がピッチコークスの粒子径よりも大きく
偏在した部分があった。
Comparative Example 4 A pitch coke electrode was produced in the same manner as in Example 4 except that heat treatment was not performed. The charge and discharge of the electrode was evaluated in the same manner as in Example 4. After charging, the discharge capacity when discharged at a constant current of 40 mA / g was 210 mAh / g per weight of pitch coke, but the discharge capacity retention rate was
It was 72%. Further, in the same manner as in Comparative Example 1, SEM
When the morphological observation of the electrode was carried out, there was no portion on the surface and cross section of the electrode where 10 or more pitch coke particles were not in contact with the binder, but on the surface of the electrode, the binder was pitch coke. There was a portion unevenly distributed that was larger than the particle diameter of.

【0035】実施例5 実施例1にて作製した正極(正極活物質30mg)に、
市販のPAN系炭素繊維(“トレカ”T−300、東レ
(株)製)1ストランド(3K:3000本)7mgを
負極にし、多孔質ポリプロピレンフィルム(セルガード
#2500、ダイセル化学(株)製)のセパレータを介
して重ね合わせて、二次電池を作製した。電解液は、1
M過塩素酸リチウムを含むプロピレンカーボネートを用
いた。
Example 5 The positive electrode (positive electrode active material 30 mg) prepared in Example 1 was
A commercially available PAN-based carbon fiber ("Torayca" T-300, manufactured by Toray Industries, Inc.) 1 strand (3K: 3000 pieces) 7 mg was used as a negative electrode, and a porous polypropylene film (Celgard # 2500, manufactured by Daicel Chemical Co., Ltd.) was prepared. A secondary battery was produced by stacking the secondary batteries via a separator. 1 electrolyte
Propylene carbonate containing M lithium perchlorate was used.

【0036】このようにして作製した二次電池を用い
て、炭素繊維重量当たりの電流密度40mA/gの定電
流で、4.3Vまで充電した。充電後、40mA/gの
定電流で放電させた時の放電容量は、負極の炭素繊維の
重量当たりで320mAh/gであり、放電容量保持率
は、89%であった。また、実施例1と同様にして、S
EMによる正極の形態観察を行ったところ、正極の表面
および断面において、結着剤が,LiCoO2 や人工黒
鉛の粒子径よりも大きく偏在した部分がなく、かつ、8
個以上のLiCoO2 や人工黒鉛粒子が結着剤に接触し
ていない部分がなかった。
Using the secondary battery thus manufactured, the battery was charged to 4.3 V at a constant current of 40 mA / g of current density per weight of carbon fiber. After charging, the discharge capacity when discharged at a constant current of 40 mA / g was 320 mAh / g based on the weight of the carbon fiber of the negative electrode, and the discharge capacity retention rate was 89%. Further, as in the first embodiment, S
When the morphology of the positive electrode was observed by EM, there was no portion where the binder was unevenly distributed over the particle size of LiCoO 2 or artificial graphite on the surface and cross section of the positive electrode, and
There was no portion where at least one LiCoO 2 or artificial graphite particle was not in contact with the binder.

【0037】比較例5 比較例1にて作製した電極を正極にする以外は、実施例
5と同様にして二次電池を作製した。実施例4と同様に
二次電池の充放電評価を行った。充電後、40mA/g
の定電流で放電させた時の放電容量は、負極の炭素繊維
の重量当たりで310mAh/gであったが、放電容量
保持率は、76%であった。また、比較例1と同様にし
て、SEMによる電極の形態観察を行ったところ、電極
の表面において、結着剤が、LiCoO2 や人工黒鉛の
粒子径よりも大きく偏在した部分があり、かつ、少なく
とも15個以上のLiCoO2 や人工黒鉛粒子が結着剤
に接触していない部分があった。
Comparative Example 5 A secondary battery was prepared in the same manner as in Example 5, except that the electrode prepared in Comparative Example 1 was used as the positive electrode. The charge / discharge evaluation of the secondary battery was performed in the same manner as in Example 4. 40 mA / g after charging
The discharge capacity when discharged at a constant current of was 310 mAh / g based on the weight of the carbon fiber of the negative electrode, but the discharge capacity retention rate was 76%. Further, when the morphology of the electrode was observed by SEM in the same manner as in Comparative Example 1, there was a portion on the surface of the electrode in which the binder was unevenly distributed larger than the particle size of LiCoO 2 or artificial graphite, and There was a portion where at least 15 or more of LiCoO 2 and artificial graphite particles were not in contact with the binder.

【0038】[0038]

【発明の効果】本発明により、放電容量特性、特にサイ
クル特性に優れた高性能二次電池の作製が可能になる。
According to the present invention, it becomes possible to manufacture a high performance secondary battery having excellent discharge capacity characteristics, particularly cycle characteristics.

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】電池電極を構成する結着剤が、電極材中に
均一に分散していることを特徴とする電極。
1. An electrode characterized in that a binder constituting a battery electrode is uniformly dispersed in an electrode material.
【請求項2】電極活物質がリチウム複合酸化物であるこ
とを特徴とする請求項1記載電極。
2. The electrode according to claim 1, wherein the electrode active material is a lithium composite oxide.
【請求項3】該リチウム複合酸化物が、Lix CoO2
(0<x≦1.0)、 Lix NiO2 (0<x≦1.0)およびLix Coy
Ni1-y 2 (0<x≦1.0、0<y≦1.0)の中
から選ばれたものであることを特徴とする請求項2記載
の電極。
3. The lithium composite oxide is Li x CoO 2
(0 <x ≦ 1.0), Li x NiO 2 (0 <x ≦ 1.0) and Li x Co y
3. The electrode according to claim 2, wherein the electrode is selected from Ni 1-y O 2 (0 <x ≦ 1.0, 0 <y ≦ 1.0).
【請求項4】電極活物質が炭素質材料であることを特徴
とする請求項1記載の電極。
4. The electrode according to claim 1, wherein the electrode active material is a carbonaceous material.
【請求項5】(1)電極活物質、導電剤、結着剤を混合
して電極材を作製する工程、 (2)上記電極材を集電体上に形成して電極を作製する
工程、 (3)上記電極を乾燥させる工程、 (4)上記電極を加圧成形し、電極材を集電体に密着さ
せる工程、 (5)上記の電極を熱処理する工程、 からなることを特徴とする請求項1記載の電極の製造方
法。
5. A step of preparing an electrode material by mixing (1) an electrode active material, a conductive agent and a binder, and (2) a step of forming the electrode material on a current collector to prepare an electrode. (3) a step of drying the electrode, (4) a step of press-molding the electrode to bring the electrode material into close contact with a current collector, and (5) a step of heat-treating the electrode. The method for manufacturing the electrode according to claim 1.
【請求項6】電極を熱処理するときの温度が、結着剤の
融点よりも高温であることを特徴とする請求項5記載の
電極の製造方法。
6. The method for producing an electrode according to claim 5, wherein the temperature for heat-treating the electrode is higher than the melting point of the binder.
【請求項7】電極活物質がリチウム複合酸化物であるこ
とを特徴とする請求項5記載電極の製造方法。
7. The method for producing an electrode according to claim 5, wherein the electrode active material is a lithium composite oxide.
【請求項8】該リチウム複合酸化物が、Lix CoO2
(0<x≦1.0)、 Lix NiO2 (0<x≦1.0)およびLix Coy
Ni1-y 2 (0<x≦1.0、0<y≦1.0)から
選ばれたものであることを特徴とする請求項5記載の電
極の製造方法。
8. The lithium composite oxide is Li x CoO 2
(0 <x ≦ 1.0), Li x NiO 2 (0 <x ≦ 1.0) and Li x Co y
The method for producing an electrode according to claim 5, wherein the electrode is selected from Ni 1-y O 2 (0 <x ≦ 1.0, 0 <y ≦ 1.0).
【請求項9】電極活物質が炭素質材料であることを特徴
とする請求項5記載の電極の製造方法。
9. The method for producing an electrode according to claim 5, wherein the electrode active material is a carbonaceous material.
【請求項10】請求項1記載の電極を用いることを特徴
とする二次電池。
10. A secondary battery comprising the electrode according to claim 1.
【請求項11】請求項2記載の電極を用いることを特徴
とする二次電池。
11. A secondary battery using the electrode according to claim 2.
【請求項12】請求項3記載の電極を用いることを特徴
とする二次電池。
12. A secondary battery using the electrode according to claim 3.
【請求項13】負極活物質に炭素質材料を用いることを
特徴とする請求項10〜12記載の二次電池。
13. The secondary battery according to claim 10, wherein a carbonaceous material is used as the negative electrode active material.
【請求項14】該炭素質材料が炭素繊維であることを特
徴とする請求項13記載の二次電池。
14. The secondary battery according to claim 13, wherein the carbonaceous material is carbon fiber.
JP5143824A 1993-06-15 1993-06-15 Electrode, method for manufacturing the same, and secondary battery using the electrode Pending JPH076752A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5143824A JPH076752A (en) 1993-06-15 1993-06-15 Electrode, method for manufacturing the same, and secondary battery using the electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5143824A JPH076752A (en) 1993-06-15 1993-06-15 Electrode, method for manufacturing the same, and secondary battery using the electrode

Publications (1)

Publication Number Publication Date
JPH076752A true JPH076752A (en) 1995-01-10

Family

ID=15347812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5143824A Pending JPH076752A (en) 1993-06-15 1993-06-15 Electrode, method for manufacturing the same, and secondary battery using the electrode

Country Status (1)

Country Link
JP (1) JPH076752A (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0935711A (en) * 1995-07-18 1997-02-07 Sumitomo Chem Co Ltd Lithium secondary battery
JPH0997603A (en) * 1995-09-29 1997-04-08 Toray Ind Inc Method for manufacturing battery electrode sheet
JP2001148242A (en) * 1998-12-24 2001-05-29 Seiko Instruments Inc Non-aqueous electrolyte secondary battery
US6475554B1 (en) 1998-03-26 2002-11-05 Tdk Corporation Method of producing electrode of non-aqueous electrolyte battery
US6667000B1 (en) 1998-03-26 2003-12-23 Tdk Corporation Method of producing an electrode
KR100589307B1 (en) * 1999-08-27 2006-06-14 삼성에스디아이 주식회사 Manufacturing method of lithium secondary battery and electrode plate for lithium secondary battery
JP2008159410A (en) * 2006-12-25 2008-07-10 Matsushita Electric Ind Co Ltd Positive electrode plate for non-aqueous secondary battery and non-aqueous secondary battery using the same
EP1947715A2 (en) 2001-04-10 2008-07-23 Mitsubishi Materials Corporation Lithium ion polymer secondary battery, its electrode and method for synthesizing polymer compound in binder used in adhesion layer thereof
JP2009266761A (en) * 2008-04-30 2009-11-12 Panasonic Corp Nonaqueous electrolyte secondary battery and its manufacturing method
WO2010029676A1 (en) * 2008-09-09 2010-03-18 パナソニック株式会社 Nonaqueous electrolyte secondary battery and method for manufacturing the same
JP2010165564A (en) * 2009-01-15 2010-07-29 Panasonic Corp Method of manufacturing non-aqueous electrolyte secondary battery, and non-aqueous electrolyte secondary battery
WO2010086911A1 (en) * 2009-01-29 2010-08-05 パナソニック株式会社 Nonaqueous electrolyte secondary battery and manufacturing method therefor
US20110195307A1 (en) * 2009-05-15 2011-08-11 Yoshiyuki Muraoka Nonaqueous electrolyte secondary battery and method for fabricating the same
JP2012004066A (en) * 2010-06-21 2012-01-05 Hitachi Vehicle Energy Ltd Secondary battery, secondary battery electrode and method of manufacturing the same
KR101154771B1 (en) * 2009-01-22 2012-06-18 파나소닉 주식회사 Rechargeable battery with nonaqueous electrolyte and process for producing the rechargeable battery
KR101236027B1 (en) * 2007-08-09 2013-02-21 파나소닉 주식회사 Rechargeable battery with nonaqueous electrolyte and process for producing the rechargeable battery
JP5506663B2 (en) * 2008-04-01 2014-05-28 パナソニック株式会社 Nonaqueous electrolyte secondary battery and manufacturing method thereof
WO2016133345A1 (en) * 2015-02-16 2016-08-25 주식회사 엘지화학 Electrode, secondary battery containing same and manufacturing method thereof
CN120356906A (en) * 2025-05-22 2025-07-22 中科融能(盐城)科技有限公司 Conductive network construction process method of solid-state battery

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0935711A (en) * 1995-07-18 1997-02-07 Sumitomo Chem Co Ltd Lithium secondary battery
JPH0997603A (en) * 1995-09-29 1997-04-08 Toray Ind Inc Method for manufacturing battery electrode sheet
US6475554B1 (en) 1998-03-26 2002-11-05 Tdk Corporation Method of producing electrode of non-aqueous electrolyte battery
US6667000B1 (en) 1998-03-26 2003-12-23 Tdk Corporation Method of producing an electrode
JP2001148242A (en) * 1998-12-24 2001-05-29 Seiko Instruments Inc Non-aqueous electrolyte secondary battery
KR100589307B1 (en) * 1999-08-27 2006-06-14 삼성에스디아이 주식회사 Manufacturing method of lithium secondary battery and electrode plate for lithium secondary battery
EP1947715A2 (en) 2001-04-10 2008-07-23 Mitsubishi Materials Corporation Lithium ion polymer secondary battery, its electrode and method for synthesizing polymer compound in binder used in adhesion layer thereof
JP2008159410A (en) * 2006-12-25 2008-07-10 Matsushita Electric Ind Co Ltd Positive electrode plate for non-aqueous secondary battery and non-aqueous secondary battery using the same
US9705159B2 (en) 2007-08-09 2017-07-11 Panasonic Intellectual Property Management Co., Ltd. Method for fabricating a nonaqueous electrolyte secondary battery
US20140331485A1 (en) * 2007-08-09 2014-11-13 Panasonic Corporation Method for fabricating a nonaqueous electrolyte secondary battery
KR101236027B1 (en) * 2007-08-09 2013-02-21 파나소닉 주식회사 Rechargeable battery with nonaqueous electrolyte and process for producing the rechargeable battery
JP5506663B2 (en) * 2008-04-01 2014-05-28 パナソニック株式会社 Nonaqueous electrolyte secondary battery and manufacturing method thereof
JP2009266761A (en) * 2008-04-30 2009-11-12 Panasonic Corp Nonaqueous electrolyte secondary battery and its manufacturing method
CN102150303A (en) * 2008-09-09 2011-08-10 松下电器产业株式会社 Nonaqueous electrolyte secondary battery and method for manufacturing the same
EP2323201A4 (en) * 2008-09-09 2012-01-11 Panasonic Corp NONAQUEOUS ELECTROLYTE RECHARGEABLE BATTERY AND METHOD FOR MANUFACTURING THE SAME
WO2010029676A1 (en) * 2008-09-09 2010-03-18 パナソニック株式会社 Nonaqueous electrolyte secondary battery and method for manufacturing the same
JP2010165564A (en) * 2009-01-15 2010-07-29 Panasonic Corp Method of manufacturing non-aqueous electrolyte secondary battery, and non-aqueous electrolyte secondary battery
KR101154771B1 (en) * 2009-01-22 2012-06-18 파나소닉 주식회사 Rechargeable battery with nonaqueous electrolyte and process for producing the rechargeable battery
US8389161B2 (en) 2009-01-22 2013-03-05 Panasonic Corporation Nonaqueous electrolyte secondary battery and method for fabricating the same
WO2010086911A1 (en) * 2009-01-29 2010-08-05 パナソニック株式会社 Nonaqueous electrolyte secondary battery and manufacturing method therefor
US20110195307A1 (en) * 2009-05-15 2011-08-11 Yoshiyuki Muraoka Nonaqueous electrolyte secondary battery and method for fabricating the same
JP2012004066A (en) * 2010-06-21 2012-01-05 Hitachi Vehicle Energy Ltd Secondary battery, secondary battery electrode and method of manufacturing the same
WO2016133345A1 (en) * 2015-02-16 2016-08-25 주식회사 엘지화학 Electrode, secondary battery containing same and manufacturing method thereof
CN120356906A (en) * 2025-05-22 2025-07-22 中科融能(盐城)科技有限公司 Conductive network construction process method of solid-state battery

Similar Documents

Publication Publication Date Title
CN101165948B (en) Anode active material, method of preparing the same, and anode and lithium battery containing the material
CN102473912B (en) Negative electrode composition for lithium secondary battery and lithium secondary battery using same
JP2006173121A (en) Cathode active material, method for producing the same, and cathode and lithium battery using the same
Yamaura et al. High voltage, rechargeable lithium batteries using newly-developed carbon for negative electrode material
JPH07122262A (en) Electrode, method for manufacturing the same, and secondary battery using the same
JPH08195199A (en) Battery electrode and secondary battery using the same
JPH0831404A (en) Electrode and secondary battery using the same
CN114600277A (en) Negative active material comprising silicon composite formed by network of conductive fibers, method of preparing the same, and lithium secondary battery comprising the same
JPH087926A (en) Non-aqueous electrolyte secondary battery
JPH08306354A (en) Electrode and non-aqueous solvent secondary battery using the same
JP2004014472A (en) Non-aqueous secondary battery
JPH08138649A (en) Non-aqueous secondary battery
WO2010082240A1 (en) Composite oxide, process for production thereof, and non-aqueous electrolyte secondary battery using the composite oxide
JPH076753A (en) Electrode, method for manufacturing the same, and secondary battery using the electrode
JPH0729598A (en) Secondary battery
JP4639410B2 (en) Negative electrode and non-aqueous electrolyte battery
JPH08203523A (en) Electrode and secondary battery using the same
JPH076763A (en) Non-aqueous solvent secondary battery
JPH0927345A (en) Lithium secondary battery
JP2003187806A (en) Non-aqueous electrolyte secondary battery
JPH09293511A (en) Electrode and non-aqueous secondary battery using the same
JPH09213331A (en) Electrode and secondary battery using the same
JP2869355B2 (en) Organic electrolyte battery
JPH08213013A (en) Electrode and secondary battery using the same
JPH08171932A (en) Secondary battery