JPH1131503A - Manufacture of pole plate and nonaqueous electrolyte secondary battery - Google Patents

Manufacture of pole plate and nonaqueous electrolyte secondary battery

Info

Publication number
JPH1131503A
JPH1131503A JP9183958A JP18395897A JPH1131503A JP H1131503 A JPH1131503 A JP H1131503A JP 9183958 A JP9183958 A JP 9183958A JP 18395897 A JP18395897 A JP 18395897A JP H1131503 A JPH1131503 A JP H1131503A
Authority
JP
Japan
Prior art keywords
active material
electrode plate
solvent
current collector
vol
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
JP9183958A
Other languages
Japanese (ja)
Other versions
JP3630529B2 (en
Inventor
Tokuaki Samitsu
徳昭 佐見津
Yorito Oohana
頼人 大花
Hiroshi Maruyama
浩 丸山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP18395897A priority Critical patent/JP3630529B2/en
Publication of JPH1131503A publication Critical patent/JPH1131503A/en
Application granted granted Critical
Publication of JP3630529B2 publication Critical patent/JP3630529B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To enhance adhesion strength between a collector and an active material layer by applying an active material paste formed by kneading electrode active material powder, a rubber binding and solvent of specific ratio the collector, and thereafter, by drying while controlling, so that the solvent evaporated is until a specific ratio is reached with in a specific time. SOLUTION: Sol-like active material paste, having proper fluidity by a solvent amount of 40 to 70 vol.% requeis a time of 0.5 to 2.5 minutes to turn into a non-fluid state of 35 vol.% by drying after application to a collector usually. Therefore, drying is conducted, for instance, by a constant temperature and constant pressure over. By this evaporation speed, the same becomes gel-like as the uniformization of binding agent distribution due to uniformaliziation of a solvent in an active paste layer is maintained, no separation of the active material and the binding agent is allowed which results from gravity difference or the like. When a positive electrode plate and a negative electrode plate by this manufacturing method are wound around into a spiral shape via a separator and are contained in a battery case, space use efficiency is high, since adhesion strength between a collector and an active material layer is strong so that a small radius of curvature is well acceptable.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、リチウム二次電池
などの非水電解液二次電池に用いられる電極板の製造方
法およびこれによって製造された電極板を用いた非水電
解液二次電池に関するものである。
The present invention relates to a method for producing an electrode plate used for a non-aqueous electrolyte secondary battery such as a lithium secondary battery, and a non-aqueous electrolyte secondary battery using the electrode plate produced by the method. It is about.

【0002】[0002]

【従来の技術】近年、電子機器の発達に伴い、小型で軽
量かつエネルギー密度が高く、さらに繰り返し充放電が
可能な二次電池の開発が要望されている。このような二
次電池として、正極にLiCoO2 などのリチウム含有
複酸化物を、負極に炭素材料をそれぞれ用いた円筒形リ
チウム二次電池が活発に研究開発されている。特に、こ
の種の電池は非水電解液を用いるため、電流特性の観点
から、電極板の表面積を大きくするため電極板をシート
状に構成している。そしてこのシート状電極板を円筒状
電池ケース内に収容率よく収容するため、そのシートを
渦巻き状に巻回する構成が多く提案されている。このよ
うなシート状電極板は、金属箔製の集電体の上に活物質
粉末が分散した活物質ペーストを厚さ数十〜数百μm均
一に塗布し、乾燥した後に、活物質の充填率を上げるた
め圧延されてなる。この活物質ペーストは、活物質粉末
と結着剤などとを水または有機溶媒に配合、混練して得
られる。
2. Description of the Related Art In recent years, with the development of electronic equipment, there has been a demand for the development of a secondary battery that is small, lightweight, has a high energy density, and can be repeatedly charged and discharged. As such a secondary battery, a cylindrical lithium secondary battery using a lithium-containing double oxide such as LiCoO 2 for a positive electrode and a carbon material for a negative electrode has been actively researched and developed. In particular, since this type of battery uses a non-aqueous electrolyte, the electrode plate is formed in a sheet shape in order to increase the surface area of the electrode plate from the viewpoint of current characteristics. In order to accommodate this sheet-shaped electrode plate in a cylindrical battery case with a good accommodation ratio, many configurations have been proposed in which the sheet is spirally wound. Such a sheet-like electrode plate is formed by applying an active material paste in which active material powder is dispersed on a metal foil current collector to a thickness of several tens to several hundreds μm, drying the material, and then filling the active material paste. Rolled to increase the rate. This active material paste is obtained by mixing and kneading the active material powder and a binder with water or an organic solvent.

【0003】円筒形電池の組立てにおいて、金属集電体
の上に厚い活物質層が塗着されたシート状電極板を小さ
な曲率半径で曲げることになるので、金属集電体と活物
質層間に大きなストレスが発生する。ここで、活物質層
中の結着剤は、活物質同士を結着すると共に、金属集電
体と活物質間を接着する役目を担っている。結着剤とし
ては、一般にペースト状態が安定なポリ四フッ化エチレ
ン樹脂ディスパージョンが用いられるが、金属集電体と
活物質間の接着強度をより強くするには、それに代えて
スチレンブタジエンゴムなどのゴム系の結着剤を主成分
とした方がよいことが判っている。
In assembling a cylindrical battery, a sheet-like electrode plate having a thick active material layer coated on a metal current collector is bent with a small radius of curvature. Big stress occurs. Here, the binder in the active material layer plays a role of binding the active materials and bonding the metal current collector and the active material. As the binder, generally, a polytetrafluoroethylene resin dispersion having a stable paste state is used, but in order to further increase the adhesive strength between the metal current collector and the active material, styrene butadiene rubber or the like is used instead. It has been found that it is better to use a rubber binder as a main component.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、本発明
者らの検討において、ゴム系の結着剤を主成分とした活
物質ペーストでは、金属集電体の上に塗着された活物質
ペーストの乾燥速度が適切でないと、金属集電体と活物
質層間の接着強度が低下して、金属集電体から活物質層
が脱落することがあるということが判った。
However, in the study of the present inventors, the active material paste containing a rubber-based binder as a main component shows that the active material paste coated on the metal current collector is not used. It has been found that if the drying rate is not appropriate, the adhesive strength between the metal current collector and the active material layer is reduced, and the active material layer may fall off from the metal current collector.

【0005】本発明は、上記問題に鑑み、集電体と活物
質層間の接着強度に優れるゴム系の結着剤を用いつつ、
その優れた接着強度を安定させることができる電極板の
製造方法およびこれによって製造された電極板を用いた
非水電解液二次電池を提供することを目的とする。
[0005] In view of the above problems, the present invention provides a rubber-based binder having excellent adhesive strength between a current collector and an active material layer.
An object of the present invention is to provide a method for manufacturing an electrode plate capable of stabilizing the excellent adhesive strength and a non-aqueous electrolyte secondary battery using the electrode plate manufactured by the method.

【0006】[0006]

【課題を解決するための手段】本発明の電極板の製造方
法は、上記目的を達成するため、電極活物質粉末とゴム
系結着剤と溶媒40〜70vol%とを混練した活物質
ペーストを集電体に塗布した後、前記集電体に塗布され
た活物質ペーストをその溶媒量が35vol%まで減少
するのに要する時間が0.5〜2.5分間となるように
溶媒の蒸発速度を制御しながら乾燥することを特徴とす
る。
In order to achieve the above object, a method for manufacturing an electrode plate according to the present invention comprises an active material paste obtained by kneading an electrode active material powder, a rubber-based binder and 40 to 70 vol% of a solvent. After being applied to the current collector, the solvent evaporation rate of the active material paste applied to the current collector is adjusted so that the time required for reducing the solvent amount to 35 vol% is 0.5 to 2.5 minutes. Characterized by drying.

【0007】本発明の電極板の製造方法によれば、溶媒
量が40〜70vol%の流動状態(ゾル状態)にある
活物質ペーストは、集電体に塗布された後、その溶媒量
が35vol%まで減少するのに要する時間が0.5分
間以上となるように活物質ペースト層表面からの溶媒の
蒸発速度が制限されるので、活物質ペースト層中の溶媒
量の均一化が維持されて結着剤の分布の均一化が維持さ
れるし、前記の時間が2.5分間以下となるように活物
質ペーストが流動状態にある時間が制限されるので、活
物質層中で活物質と結着剤とが重力差などで分離するこ
となく結着剤の分布の均一化が維持される。そして、集
電体に塗布された活物質ペーストの溶媒量が35vol
%まで減少すると、その活物質ペーストが非流動状態
(ゲル状態)になるので、その後の溶媒の蒸発速度の大
小に係わらず活物質ペースト層中の結着剤の移動は生じ
なくなる。従って、活物質層の集電体表面近傍の結着剤
の量や分布が均一となるので、集電体と活物質層間の接
着強度に優れるゴム系の結着剤を用いつつ、その優れた
接着強度を安定させることができる。
According to the method for manufacturing an electrode plate of the present invention, the active material paste in a fluid state (sol state) having a solvent amount of 40 to 70 vol% is applied to a current collector, and then the solvent amount is 35 vol. %, The rate of evaporation of the solvent from the surface of the active material paste layer is limited so that the time required to reduce the amount to 0.5% or more is maintained, so that the amount of solvent in the active material paste layer is kept uniform. Uniform distribution of the binder is maintained, and the time during which the active material paste is in a fluidized state is limited so that the above-mentioned time is 2.5 minutes or less. Uniform distribution of the binder is maintained without separation from the binder due to a gravity difference or the like. Then, the solvent amount of the active material paste applied to the current collector is 35 vol.
%, The active material paste becomes in a non-fluid state (gel state), so that no movement of the binder in the active material paste layer occurs regardless of the subsequent evaporation rate of the solvent. Therefore, since the amount and distribution of the binder near the current collector surface of the active material layer become uniform, while using a rubber-based binder having excellent adhesive strength between the current collector and the active material layer, the excellent Adhesive strength can be stabilized.

【0008】活物質層が流動状態にある時間が0.5分
間より短いと、活物質層中の結着剤が雰囲気側に移動す
るマイグレーションが発生して、集電体側の結着剤が不
足する結果、集電体と活物質層間の接着強度が低下し好
ましくなく、前記時間が2.5分間より長いと、活物質
層中で活物質と結着剤とが重力差などで徐々に分離して
結着剤の分布が不均一になる結果、結着剤が不足した部
分の集電体と活物質層間の接着強度が低下し好ましくな
い。なお、活物質ペーストの当初の溶媒量が40vol
%に満たないと、活物質ペーストの流動性が小さすぎて
塗布が困難となり好ましくなく、前記溶媒量が70vo
l%を越えると、流動性が大きすぎて均一な厚さでの塗
布が困難となり好ましくない。
If the time during which the active material layer is in a fluid state is shorter than 0.5 minutes, migration occurs in which the binder in the active material layer moves to the atmosphere side, and the binder on the current collector side runs short. As a result, the adhesive strength between the current collector and the active material layer is lowered, which is not preferable. If the time is longer than 2.5 minutes, the active material and the binder are gradually separated in the active material layer due to a gravity difference or the like. As a result, the distribution of the binder becomes non-uniform. As a result, the adhesive strength between the current collector and the active material layer in the portion where the binder is insufficient is undesirably reduced. Note that the initial solvent amount of the active material paste was 40 vol.
%, The fluidity of the active material paste is too small to apply, which is not preferable.
If it exceeds 1%, the fluidity is too large and it is difficult to apply a uniform thickness, which is not preferable.

【0009】本発明の非水電解液二次電池は、前記本発
明の電極板の製造方法により製造された正極板または負
極板を用い、正極板と負極板とがセパレータを介して渦
巻き状に巻回されて円筒状の電池ケースに組み込まれて
いることを特徴とする。
A nonaqueous electrolyte secondary battery of the present invention uses a positive electrode plate or a negative electrode plate manufactured by the above-described method of manufacturing an electrode plate of the present invention, and the positive electrode plate and the negative electrode plate are spirally interposed via a separator. The battery is wound and incorporated in a cylindrical battery case.

【0010】本発明の非水電解液二次電池によれば、前
記本発明の電極板の製造方法による正極板または負極板
は、集電体と活物質層間の接着強度が強く安定している
ので、小さな曲率半径で曲げられても、活物質層が剥離
することがない。従って、正極板と負極板とを、セパレ
ータを介して渦巻き状に巻回して円筒状の電池ケース内
に空間利用効率よく組み込むことができる。また、円筒
状電池ケースの中心軸近傍の空間にも電極を配すること
ができるので、特に直径の小さな円筒形の非水電解液二
次電池において有用である。
According to the non-aqueous electrolyte secondary battery of the present invention, the positive electrode plate or the negative electrode plate produced by the method for producing an electrode plate of the present invention has a strong and stable adhesive strength between the current collector and the active material layer. Therefore, even if the active material layer is bent with a small radius of curvature, the active material layer does not peel off. Therefore, the positive electrode plate and the negative electrode plate can be spirally wound with the separator interposed therebetween, and can be efficiently incorporated into the cylindrical battery case. Further, the electrodes can be arranged in the space near the central axis of the cylindrical battery case, which is particularly useful for a cylindrical non-aqueous electrolyte secondary battery having a small diameter.

【0011】[0011]

【発明の実施の形態】本発明の実施形態を図面に基づい
て以下に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings.

【0012】本発明の電極板の製造方法の一実施形態
は、活物質ペーストを得る第1工程と、活物質ペースト
を集電体に塗布する第2工程と、集電体に塗布された活
物質ペーストをその溶媒量が35vol%以下になるま
で乾燥する第3工程と、前記の活物質ペーストをほぼ完
全に乾燥する第4工程と、乾燥して得られたものを圧延
・裁断して電極板を得る第5工程とからなる。前記の第
2〜第4工程は、図1に示す製造装置にて行われる。
One embodiment of the method for manufacturing an electrode plate according to the present invention includes a first step of obtaining an active material paste, a second step of applying the active material paste to a current collector, and an active material applied to the current collector. A third step of drying the material paste until the amount of the solvent is 35 vol% or less, a fourth step of drying the active material paste almost completely, and rolling and cutting the dried product to obtain an electrode. And a fifth step of obtaining a plate. The above second to fourth steps are performed by the manufacturing apparatus shown in FIG.

【0013】先ず、製造装置は、図1に示すように、テ
ープ状の集電体12(13)を繰出す繰出し機14と、
走行している集電体12(13)を弛まないように支持
する4つのローラ15と、走行している集電体12(1
3)に活物質ペーストを塗布する活物質コーター16
と、活物質コーター16の走行方向下流に配され槽内の
雰囲気の温度と湿度とを制御する恒温恒湿槽17と、恒
温恒湿槽17の走行方向下流に配され集電体12(1
3)に塗布された活物質ペーストをほぼ完全に乾燥する
乾燥炉18と、ほぼ完全に乾燥された集電体12(1
3)を走行速度可変に巻取る巻取り機19とを備えてい
る。
First, as shown in FIG. 1, the manufacturing apparatus comprises a feeding machine 14 for feeding a tape-shaped current collector 12 (13);
Four rollers 15 for supporting the running current collector 12 (13) so as not to loosen, and the running current collector 12 (1
3) Active material coater 16 for applying active material paste
A constant temperature / humidity chamber 17 arranged downstream of the active material coater 16 in the traveling direction to control the temperature and humidity of the atmosphere in the chamber; and a current collector 12 (1) arranged downstream of the constant temperature / humidity chamber 17 in the traveling direction.
The drying furnace 18 for drying the active material paste applied to 3) almost completely and the current collector 12 (1 for almost completely dried)
And 3) a winder 19 that winds at a variable traveling speed.

【0014】恒温恒湿槽17は、前記第3工程に用いら
れるもので、集電体12(13)の走行方向長さが50
0mmある槽内の雰囲気の温度と湿度とを制御すること
によって、集電体12(13)に塗布された活物質ペー
ストをその溶媒の蒸発速度を制御しながら乾燥するよう
に構成されている。また、乾燥炉18は、前記第4工程
に用いられるもので、加熱ヒータとファンとを内蔵して
いる。
The constant temperature / humidity chamber 17 is used in the third step, and has a length in the traveling direction of the current collector 12 (13) of 50%.
By controlling the temperature and humidity of the atmosphere in the tank of 0 mm, the active material paste applied to the current collector 12 (13) is dried while controlling the evaporation rate of the solvent. The drying furnace 18 is used in the fourth step, and includes a heater and a fan.

【0015】第1工程は、正極活物質ペーストおよび負
極活物質ペーストそれぞれを得る工程である。
The first step is a step of obtaining each of a positive electrode active material paste and a negative electrode active material paste.

【0016】正極活物質ペーストは、正極活物質として
LiCoO2 粉末を55wt%と、導電材としてカーボ
ンブラックを1.5wt%、結着剤としてスチレンブタ
ジエンゴム3.0wt%と、増粘剤としてカルボキシル
メチルセルロースを0.5wt%、ペースト溶媒として
水を40wt%、配合して混練して得た。得られた正極
活物質ペーストの水分は体積率で64vol%であっ
た。正極活物質は、LiCoO2 の他に、例えばLiN
iO2 、LiMn2 4 でもよい。
The positive electrode active material paste contains 55% by weight of LiCoO 2 powder as a positive electrode active material, 1.5% by weight of carbon black as a conductive material, 3.0% by weight of styrene butadiene rubber as a binder, and carboxyl as a thickener. 0.5 wt% of methylcellulose and 40 wt% of water as a paste solvent were blended and kneaded. The water content of the obtained positive electrode active material paste was 64 vol% in volume ratio. The positive electrode active material is, for example, LiN in addition to LiCoO 2.
iO 2 or LiMn 2 O 4 may be used.

【0017】負極活物質ペーストは、負極活物質として
黒鉛粉末を53wt%、結着剤としてスチレンブタジエ
ンゴムを6.0wt%、増粘剤としてカルボキシルメチ
ルセルロースを1.0wt%、ペースト溶媒として水を
40wt%、配合し混練して得た。得られた負極活物質
ペーストの水分は体積率で53vol%であった。負極
活物質は、002面の格子面間隔が3.35〜3.80
Åの炭素材粉末が好ましく、前記黒鉛粉末の他に、例え
ば石油コークス、クレゾール樹脂焼成炭素粉末、フラン
樹脂焼成炭素粉末、ポリアクリロニトリル樹脂焼成炭素
粉末、気相成長炭素粉末、メソフェーズピッチ焼成炭素
粉末でもよい。
The negative electrode active material paste contains 53% by weight of graphite powder as a negative electrode active material, 6.0% by weight of styrene butadiene rubber as a binder, 1.0% by weight of carboxymethyl cellulose as a thickener, and 40% by weight of water as a paste solvent. %, Blended and kneaded. The water content of the obtained negative electrode active material paste was 53 vol% in volume ratio. The negative electrode active material has a lattice spacing of 002 planes of 3.35 to 3.80.
炭素 carbon material powder is preferable, in addition to the graphite powder, for example, petroleum coke, cresol resin fired carbon powder, furan resin fired carbon powder, polyacrylonitrile resin fired carbon powder, vapor grown carbon powder, mesophase pitch fired carbon powder Good.

【0018】第2工程では、厚さ20μmのAl箔製の
集電体12に正極活物質ペーストを、厚さ16μmのC
u箔製の集電体13に負極活物質ペーストを、それぞれ
厚さ約150μm均一に連続塗布した。集電体12(1
3)の走行速度は、巻取り機19にて200〜1000
mm/分の範囲で設定した。活物質コーター16は、前
記に設定された走行速度に対応して活物質の吐出速度を
制御して、一定の塗布厚さ約150μmを確保するよう
に構成されている。
In the second step, a cathode active material paste is applied to a 20 μm thick current collector 12 made of Al foil, and a 16 μm thick C
The negative electrode active material paste was continuously and uniformly applied to a thickness of about 150 μm on the current collector 13 made of u foil. Current collector 12 (1
The traveling speed of 3) is 200 to 1000 by the winder 19.
It was set in the range of mm / min. The active material coater 16 is configured to control the discharge speed of the active material in accordance with the traveling speed set as described above, so as to secure a constant coating thickness of about 150 μm.

【0019】第3工程では、恒温恒湿槽17の槽内雰囲
気の温度と湿度とを制御して、集電体12(13)に塗
布された活物質ペーストを、その水分量(溶媒量)が3
5vol%まで減少するのに要する時間が0.5〜2.
5分間となるように、水分の蒸発速度を可変制御しなが
ら乾燥した。具体的には、負極集電体13の実施例1、
2および3それぞれの走行速度1000、500および
200mm/分間に対応して、長さ500mmの恒温恒
湿槽17内を通過した直後の水分量が35±1vol%
となるように槽内雰囲気の温度と湿度とを可変制御し
た。表1に示すように、実施例1、2および3では、前
記の時間をそれぞれ0.5、1.0および2.5分間と
した。なお、正極集電体12における前記の時間は、一
定の1.0分間とした。
In the third step, the active material paste applied to the current collector 12 (13) is controlled by controlling the temperature and humidity of the atmosphere in the constant temperature and humidity chamber 17 so that the amount of water (the amount of solvent) Is 3
The time required to reduce to 5 vol% is 0.5-2.
Drying was performed while variably controlling the evaporation rate of water so as to obtain 5 minutes. Specifically, Example 1 of the negative electrode current collector 13,
Corresponding to the traveling speeds of 1000 and 500 and 200 mm / min for 2 and 3 respectively, the water content immediately after passing through the constant temperature and humidity chamber 17 having a length of 500 mm is 35 ± 1 vol%.
The temperature and humidity of the atmosphere in the tank were variably controlled so that As shown in Table 1, in Examples 1, 2 and 3, the times were set to 0.5, 1.0 and 2.5 minutes, respectively. In addition, the said time in the positive electrode current collector 12 was made into fixed 1.0 minute.

【0020】第4工程では、乾燥炉18の炉内温度を約
150℃に設定して、集電体12(13)に塗布され第
3工程で約35vol%まで乾燥された活物質ペースト
の水分をほぼ完全に除去し、自然に冷却して巻取り機1
9に巻き取った。
In the fourth step, the temperature inside the drying furnace 18 is set to about 150 ° C., and the water content of the active material paste applied to the current collector 12 (13) and dried to about 35 vol% in the third step is obtained. Is almost completely removed, and is naturally cooled to take up the winder 1
9 rolled up.

【0021】第5工程では、乾燥して得られたものを活
物質の充填密度を上げるために圧延し、最後に電池一個
分に使用する寸法に裁断して正極板、負極板それぞれの
電極板が得られた。
In the fifth step, the product obtained by drying is rolled in order to increase the packing density of the active material, and finally cut into dimensions to be used for one battery, and each of the positive electrode plate and the negative electrode plate is cut. was gotten.

【0022】[0022]

【表1】 [Table 1]

【0023】このようにして得られた負極板の実施例1
〜3の活物質層の接着強度を連続荷重式引掻強度試験機
(JISK6718)を用いた引掻強度で評価した。こ
の試験は、幅5mmの引掻刃を活物質層の上面に垂直に
押圧しながら引掻速度600mm/分で引掻いて剥離の
有無を判定するもので、試料に印加する荷重を段階的に
増加させて印加し、活物質層の剥離が発生したときの最
低荷重がその試料の引掻強度となる。評価結果を比較例
1、2と共に、表1にまとめた。
Example 1 of the negative electrode plate thus obtained
The adhesive strength of the active material layers of Nos. 1 to 3 was evaluated by a scratch strength using a continuous load type scratch strength tester (JIS K6718). This test is to determine the presence or absence of peeling by scratching at a scratching speed of 600 mm / min while vertically pressing a scratching blade having a width of 5 mm against the upper surface of the active material layer. The applied load is increased, and the minimum load when the active material layer peels off is the scratch strength of the sample. Table 1 summarizes the evaluation results together with Comparative Examples 1 and 2.

【0024】表1に示すように、負極板は、集電体13
に塗布された活物質ペーストをその水分量が35vol
%まで減少するのに要する時間が0.5〜2.5分間の
範囲において、活物質層の集電体13との接着強度が強
く安定していることが判る。
As shown in Table 1, the negative electrode plate was formed by a current collector 13
The water content of the active material paste applied to the
%, The adhesive strength of the active material layer to the current collector 13 is strong and stable in the range of 0.5 to 2.5 minutes.

【0025】また、前記時間が0.3分間の比較例1や
前記時間が4.0分間の比較例2のものは、共に接着強
度が低下している。
The adhesive strength of Comparative Example 1 in which the time was 0.3 minutes and Comparative Example 2 in which the time was 4.0 minutes were both reduced.

【0026】本発明の非水電解液二次電池の一実施形態
は、前記実施形態による正極板および負極板を用いたも
ので、図2に示すような直径17mm、長さ50mmの
円筒型リチウム二次電池であり、極板群と、電解液と、
これらを収容する電池ケースとからなる。
One embodiment of the nonaqueous electrolyte secondary battery of the present invention uses the positive electrode plate and the negative electrode plate according to the above embodiment, and has a cylindrical lithium 17 mm diameter and 50 mm length as shown in FIG. A secondary battery, an electrode group, an electrolytic solution,
And a battery case for accommodating them.

【0027】極板群は、シート状の正極板1と、シート
状の負極板3と、正極板1と負極板3間を絶縁するシー
ト状のセパレータ5と、正極リード2と、負極リード4
と、上部絶縁板6と、下部絶縁板7とからなる。これら
正極板1と負極板3とが、多孔質ポリプロピレンフィル
ム製のセパレータ5を介して重ねられ、渦巻き状に巻回
されて、円筒型の電池ケース内にきっちりと収容されて
いる。特に、負極板3は上記実施例2のものである。
The electrode group includes a sheet-like positive electrode plate 1, a sheet-like negative electrode plate 3, a sheet-like separator 5 insulating between the positive electrode plate 1 and the negative electrode plate 3, a positive electrode lead 2, and a negative electrode lead 4.
And an upper insulating plate 6 and a lower insulating plate 7. The positive electrode plate 1 and the negative electrode plate 3 are stacked with a separator 5 made of a porous polypropylene film interposed therebetween, spirally wound, and housed tightly in a cylindrical battery case. In particular, the negative electrode plate 3 is that of the second embodiment.

【0028】電解液は、炭酸エチレンと炭酸ジエチルと
プロピオン酸メチルとの等体積混合有機溶媒にLiPF
6 を1.5mol/literの濃度に溶解した非水電
解液からなる。この非水電解液は、電池ケース内に収容
され、正極活物質層および負極活物質層中の連続した空
隙中にも充填されて、電池反応において、多孔質なセパ
レータ5の微小孔を通しての正極板1と負極板3間のL
iイオンの移動を担う。
The electrolytic solution was prepared by mixing LiPF in an organic solvent mixture of equal volume of ethylene carbonate, diethyl carbonate and methyl propionate.
6 is a non-aqueous electrolyte in which 1.5 mol / liter is dissolved. This non-aqueous electrolyte is accommodated in a battery case and filled in continuous voids in the positive electrode active material layer and the negative electrode active material layer. In the battery reaction, the positive electrode passes through the fine pores of the porous separator 5. L between plate 1 and negative plate 3
Responsible for i-ion transfer.

【0029】電池ケースは、耐有機電解液性のステンレ
ス鋼板を深絞り成形して得たケース本体8と、安全弁1
1を設けた封口板10と、正極外部端子となる封口板1
0と負極外部端子となるケース本体8との間を絶縁しガ
スシールする絶縁ガスケット9とからなる。
The battery case includes a case body 8 obtained by deep drawing an stainless steel sheet having resistance to organic electrolyte and a safety valve 1.
And a sealing plate 1 serving as a positive electrode external terminal
0 and an insulating gasket 9 for insulating and gas-sealing between the case body 8 and the negative electrode external terminal.

【0030】この円筒型リチウム二次電池によれば、正
極板と負極板とを小さな曲率半径で曲げても活物質層が
剥離することなく、正極板と負極板とをセパレータを介
して渦巻き状に巻回して円筒状の電池ケース内に空間利
用効率よく組み込むことができた。
According to this cylindrical lithium secondary battery, even when the positive electrode plate and the negative electrode plate are bent with a small radius of curvature, the active material layer does not peel off, and the positive electrode plate and the negative electrode plate are spirally interposed via the separator. And efficiently incorporated into the cylindrical battery case.

【0031】上記実施形態では、結着剤としてスチレン
ブタジエンゴムを用いたが、本発明はこれに限定され
ず、他のゴム系結着剤、例えばイソプレンゴム、クロロ
プレンゴム、アクリルゴム、ウレタンゴム、シリコーン
ゴム、フッ素ゴムでもよい。
In the above embodiment, styrene butadiene rubber was used as the binder, but the present invention is not limited to this, and other rubber binders such as isoprene rubber, chloroprene rubber, acrylic rubber, urethane rubber, Silicone rubber or fluorine rubber may be used.

【0032】また上記実施形態では、ペースト溶媒とし
て水を用いたが、本発明はこれに限定されず、適当な蒸
気圧を有する一般的な有機溶媒、例えばN−メチルピロ
リドン、キシレン、トルエン、アセトン、メチルエチル
ケトン、メチルイソブチルケトン、キクロヘキサン、エ
タノール、メタノール、酢酸メチル、酢酸エチル、酢酸
ブチル、塩化メチレン、塩化エチレンでもよい。
In the above embodiment, water was used as the paste solvent. However, the present invention is not limited to this, and general organic solvents having an appropriate vapor pressure, for example, N-methylpyrrolidone, xylene, toluene, acetone , Methyl ethyl ketone, methyl isobutyl ketone, cyclohexane, ethanol, methanol, methyl acetate, ethyl acetate, butyl acetate, methylene chloride, ethylene chloride.

【0033】円筒型リチウム二次電池の上記実施形態で
は、正極板および負極板共に、前記本発明の電極板の製
造方法を適用したが、正極板または負極板のうち集電体
と活物質層間の接着強度の弱い方の極板にのみ前記本発
明の電極板の製造方法を適用しても、大きな効果を得ら
れる。
In the above-described embodiment of the cylindrical lithium secondary battery, the method of manufacturing the electrode plate of the present invention is applied to both the positive electrode plate and the negative electrode plate. Even if the method for manufacturing an electrode plate of the present invention is applied only to the electrode plate having a weaker adhesive strength, a great effect can be obtained.

【0034】また上記実施形態では、正極活物質および
負極活物質がLiを可逆的に吸蔵、放出する電極板の製
造方法とこれによる電極板を用いたリチウム二次電池に
ついて述べたが、Liの代わりにH、NaまたはKを可
逆的に吸蔵、放出する電極板の製造方法とこれによる電
極板を用いた非水溶液二次電池にも適用できる。
In the above embodiment, the method of manufacturing an electrode plate in which the positive electrode active material and the negative electrode active material occlude and release Li reversibly and a lithium secondary battery using the electrode plate according to the method have been described. Alternatively, the present invention can be applied to a method of manufacturing an electrode plate that reversibly stores and releases H, Na, or K, and a non-aqueous solution secondary battery using the electrode plate.

【0035】[0035]

【発明の効果】本発明の電極板の製造方法によれば、溶
媒量が40〜70vol%の流動状態(ゾル状態)にあ
る活物質ペーストは、集電体に塗布された後、その溶媒
量が35vol%まで減少するのに要する時間が0.5
分間以上となるように活物質ペースト層表面からの溶媒
の蒸発速度が制限されるので、活物質ペースト層中の溶
媒量の均一化が維持されて結着剤の分布の均一化が維持
されるし、前記の時間が2.5分間以下となるように活
物質ペーストが流動状態にある時間が制限されるので、
活物質層中で活物質と結着剤とが重力差などで分離する
ことなく結着剤の分布の均一化が維持される。そして、
集電体に塗布された活物質ペーストの溶媒量が35vo
l%まで減少すると、その活物質ペーストが非流動状態
(ゲル状態)になるので、その後の溶媒の蒸発速度の大
小に係わらず活物質ペースト層中の結着剤の移動は生じ
なくなる。従って、活物質層の集電体表面近傍の結着剤
の量や分布が均一となるので、集電体と活物質層間の接
着強度に優れるゴム系の結着剤を用いつつ、その優れた
接着強度を安定させることができる。
According to the method for manufacturing an electrode plate of the present invention, the active material paste in a fluid state (sol state) having a solvent amount of 40 to 70 vol% is applied to a current collector and then the solvent amount is reduced. Takes 0.5% to decrease to 35% by volume.
The evaporation rate of the solvent from the surface of the active material paste layer is limited so as to be more than one minute, so that the amount of the solvent in the active material paste layer is kept uniform and the distribution of the binder is kept uniform. Since the time during which the active material paste is in a fluidized state is limited so that the above-mentioned time is 2.5 minutes or less,
The uniform distribution of the binder is maintained without the active material and the binder being separated in the active material layer due to a gravity difference or the like. And
Solvent amount of active material paste applied to current collector is 35 vo
When the active material paste is reduced to 1%, the active material paste becomes in a non-fluid state (gel state), so that the binder does not move in the active material paste layer regardless of the subsequent evaporation rate of the solvent. Therefore, since the amount and distribution of the binder near the current collector surface of the active material layer become uniform, while using a rubber-based binder having excellent adhesive strength between the current collector and the active material layer, the excellent Adhesive strength can be stabilized.

【0036】本発明の非水電解液二次電池によれば、前
記本発明の電極板の製造方法による正極板または負極板
は、集電体と活物質層間の接着強度が強く安定している
ので、小さな曲率半径で曲げられても、活物質層が剥離
することがない。従って、正極板と負極板とを、セパレ
ータを介して渦巻き状に巻回して円筒状の電池ケース内
に空間利用効率よく組み込むことができる。
According to the non-aqueous electrolyte secondary battery of the present invention, the positive electrode plate or the negative electrode plate produced by the method for producing an electrode plate of the present invention has a strong and stable adhesive strength between the current collector and the active material layer. Therefore, even if the active material layer is bent with a small radius of curvature, the active material layer does not peel off. Therefore, the positive electrode plate and the negative electrode plate can be spirally wound with the separator interposed therebetween, and can be efficiently incorporated into the cylindrical battery case.

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

【図1】本発明の電極板の製造方法の一実施形態を示す
概念図。
FIG. 1 is a conceptual diagram showing one embodiment of a method for manufacturing an electrode plate of the present invention.

【図2】本発明の非水電解液二次電池の一実施形態を示
す概略断面図。
FIG. 2 is a schematic sectional view showing one embodiment of a non-aqueous electrolyte secondary battery of the present invention.

【符号の説明】[Explanation of symbols]

1 正極板 3 負極板 1 positive electrode plate 3 negative electrode plate

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 電極活物質粉末とゴム系結着剤と溶媒4
0〜70vol%とを混練した活物質ペーストを集電体
に塗布した後、前記集電体に塗布された活物質ペースト
をその溶媒量が35vol%まで減少するのに要する時
間が0.5〜2.5分間となるように溶媒の蒸発速度を
制御しながら乾燥することを特徴とする電極板の製造方
法。
1. An electrode active material powder, a rubber binder and a solvent
After the active material paste kneaded with 0 to 70 vol% is applied to the current collector, the time required for the active material paste applied to the current collector to reduce the solvent amount to 35 vol% is 0.5 to 0.5 vol%. A method for producing an electrode plate, characterized in that drying is performed while controlling the evaporation rate of the solvent so as to be 2.5 minutes.
【請求項2】 請求項1記載の電極板の製造方法により
製造された正極板または負極板を用い、正極板と負極板
とがセパレータを介して渦巻き状に巻回されて円筒状の
電池ケースに組み込まれていることを特徴とする非水電
解液二次電池。
2. A cylindrical battery case using a positive electrode plate or a negative electrode plate manufactured by the method for manufacturing an electrode plate according to claim 1, wherein the positive electrode plate and the negative electrode plate are spirally wound via a separator. Non-aqueous electrolyte secondary battery characterized by being incorporated in a battery.
JP18395897A 1997-07-09 1997-07-09 Nonaqueous electrolyte secondary battery and method of manufacturing electrode plate thereof Expired - Fee Related JP3630529B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18395897A JP3630529B2 (en) 1997-07-09 1997-07-09 Nonaqueous electrolyte secondary battery and method of manufacturing electrode plate thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18395897A JP3630529B2 (en) 1997-07-09 1997-07-09 Nonaqueous electrolyte secondary battery and method of manufacturing electrode plate thereof

Publications (2)

Publication Number Publication Date
JPH1131503A true JPH1131503A (en) 1999-02-02
JP3630529B2 JP3630529B2 (en) 2005-03-16

Family

ID=16144803

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18395897A Expired - Fee Related JP3630529B2 (en) 1997-07-09 1997-07-09 Nonaqueous electrolyte secondary battery and method of manufacturing electrode plate thereof

Country Status (1)

Country Link
JP (1) JP3630529B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004063457A (en) * 2002-06-05 2004-02-26 Mitsubishi Chemicals Corp Manufacturing method of carbon material for electrode
JP2010199043A (en) * 2009-02-27 2010-09-09 Mitsubishi Heavy Ind Ltd Method of manufacturing negative electrode for secondary battery, and nonaqueous secondary battery
JP2011076910A (en) * 2009-09-30 2011-04-14 Nippon Zeon Co Ltd Slurry composition for electrode
JP2012028164A (en) * 2010-07-23 2012-02-09 Ngk Insulators Ltd Drying furnace for electrode coating film for lithium ion battery
WO2013099569A1 (en) * 2011-12-27 2013-07-04 東レエンジニアリング株式会社 Current collector electrode film coating drying method
JP5259875B1 (en) * 2012-07-19 2013-08-07 日本碍子株式会社 Battery electrode coating film drying method and drying furnace
WO2016103667A1 (en) * 2014-12-26 2016-06-30 三洋電機株式会社 Cylindrical battery
CN113646094A (en) * 2019-12-09 2021-11-12 株式会社Lg新能源 Apparatus for manufacturing electrode for secondary battery including heating part for heating electrode current collector before coating electrode active material slurry and method for manufacturing electrode for secondary battery including heating process
US11837709B2 (en) 2019-12-09 2023-12-05 Lg Energy Solution, Ltd. Manufacturing apparatus of electrode for secondary battery comprising heating part and manufacturing method of electrode for secondary battery comprising heating process, for heating electrode current collector before coating with electrode active material slurry

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004063457A (en) * 2002-06-05 2004-02-26 Mitsubishi Chemicals Corp Manufacturing method of carbon material for electrode
JP2010199043A (en) * 2009-02-27 2010-09-09 Mitsubishi Heavy Ind Ltd Method of manufacturing negative electrode for secondary battery, and nonaqueous secondary battery
JP2011076910A (en) * 2009-09-30 2011-04-14 Nippon Zeon Co Ltd Slurry composition for electrode
JP2012028164A (en) * 2010-07-23 2012-02-09 Ngk Insulators Ltd Drying furnace for electrode coating film for lithium ion battery
WO2013099569A1 (en) * 2011-12-27 2013-07-04 東レエンジニアリング株式会社 Current collector electrode film coating drying method
JP5259875B1 (en) * 2012-07-19 2013-08-07 日本碍子株式会社 Battery electrode coating film drying method and drying furnace
WO2016103667A1 (en) * 2014-12-26 2016-06-30 三洋電機株式会社 Cylindrical battery
CN113646094A (en) * 2019-12-09 2021-11-12 株式会社Lg新能源 Apparatus for manufacturing electrode for secondary battery including heating part for heating electrode current collector before coating electrode active material slurry and method for manufacturing electrode for secondary battery including heating process
US11837709B2 (en) 2019-12-09 2023-12-05 Lg Energy Solution, Ltd. Manufacturing apparatus of electrode for secondary battery comprising heating part and manufacturing method of electrode for secondary battery comprising heating process, for heating electrode current collector before coating with electrode active material slurry

Also Published As

Publication number Publication date
JP3630529B2 (en) 2005-03-16

Similar Documents

Publication Publication Date Title
KR100963981B1 (en) Jelly-roll Having Active Material Layer with Different Loading Amount
CN110299515B (en) Positive electrode active material, preparation method thereof, positive electrode and battery
US20100239914A1 (en) Cathode for lithium battery
JP5196982B2 (en) Non-aqueous electrolyte battery
WO2008029719A1 (en) Nonaqueous electrolytic secondary cell
WO2000033404A1 (en) Lithium secondary cell and method for manufacturing the same
JP2005123047A (en) Lithium secondary battery and manufacturing method thereof
JP5181585B2 (en) Method for producing negative electrode for lithium secondary battery
JP3630529B2 (en) Nonaqueous electrolyte secondary battery and method of manufacturing electrode plate thereof
US9899673B2 (en) Negative electrode material, negative electrode for lithium ion secondary battery, lithium ion secondary battery, and method of manufacturing the same
JP2002170556A (en) Method for manufacturing electrode plate of secondary battery
JP3139390B2 (en) Negative electrode for non-aqueous electrolyte secondary battery, method for producing the same, and non-aqueous electrolyte secondary battery using the same
JP2020035682A (en) Non-aqueous electrolyte secondary battery and manufacturing method of non-aqueous electrolyte secondary battery
JP2002367601A (en) Manufacturing method of electrode made of continuously coated porous current collector, and design of cell having above electrode
KR20160123050A (en) Method of manufacturing lithium secondary battery
US20200152992A1 (en) Electrode for solid state battery, solid state battery and manufacturing method of electrode for solid state battery
JP2002203603A (en) Gel electrolyte battery
EP4113658A1 (en) Method for manufacturing electrode for lithium secondary battery
JPH1027601A (en) Nonaqueous electrolyte secondary battery
CN112670517A (en) Electrode for lithium ion secondary battery and lithium ion secondary battery
JPH1064522A (en) Manufacture of sheet-like electrode plate and nonaqueous electrolyte battery
JPH11339772A (en) Electrode plate for secondary battery and its manufacture
JPH05182657A (en) Negative electrode and manufacture thereof for lithium secondary battery
CN111987277B (en) Porous carrier and electrochemical device separation membrane
JP4316461B2 (en) Non-aqueous electrolyte secondary battery electrode and non-aqueous electrolyte secondary battery

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040730

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040817

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20041004

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20041116

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20041214

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071224

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081224

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091224

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091224

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101224

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees