JP2000182623A - Electrolytic copper foil, copper foil for current collector of secondary battery, and secondary battery - Google Patents

Electrolytic copper foil, copper foil for current collector of secondary battery, and secondary battery

Info

Publication number
JP2000182623A
JP2000182623A JP10353213A JP35321398A JP2000182623A JP 2000182623 A JP2000182623 A JP 2000182623A JP 10353213 A JP10353213 A JP 10353213A JP 35321398 A JP35321398 A JP 35321398A JP 2000182623 A JP2000182623 A JP 2000182623A
Authority
JP
Japan
Prior art keywords
copper foil
secondary battery
current collector
electrolytic copper
ppm
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
JP10353213A
Other languages
Japanese (ja)
Other versions
JP3850155B2 (en
Inventor
Koichi Harigaya
浩一 張ヶ谷
Hideo Noguchi
英男 野口
Katsumi Kobayashi
勝己 小林
Kazuyoshi Aso
和義 阿曽
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.)
Nippon Denkai Co Ltd
Original Assignee
Nippon Denkai 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 Nippon Denkai Co Ltd filed Critical Nippon Denkai Co Ltd
Priority to JP35321398A priority Critical patent/JP3850155B2/en
Publication of JP2000182623A publication Critical patent/JP2000182623A/en
Application granted granted Critical
Publication of JP3850155B2 publication Critical patent/JP3850155B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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)
  • Cell Electrode Carriers And Collectors (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an electrolytic copper foil used as a current collector of a secondary battery, excellent in the tensile strength and in the rate of elongation at a room temp. and after being heated and a secondary battery equipped with a current collector consisting of such copper foil excellent in overcharging test characteristics. SOLUTION: An electrolytic copper foil containing not more than 5 ppm carbon and not more than 3 ppm sulfur is used as a current collector of a secondary battery, which is furnished with a negative electrode and positive electrode of such a structure that an electrode constituting substance layer is formed on the surface of current collector in plane form, wherein at least one of the plane current collectors of the positive and negative electrodes consists of the electrolytic copper foil.

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】本発明は引張り強さ、伸び率
に優れた電解銅箔、この銅箔からなる二次電池の集電体
用銅箔及びこの銅箔を用いた二次電池に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic copper foil having excellent tensile strength and elongation, a copper foil for a current collector of a secondary battery comprising the copper foil, and a secondary battery using the copper foil.

【0002】[0002]

【従来の技術】近年、携帯電子機器の進展は著しく、例
えば、電話、ノート型パソコン、カメラ一体型VTR、
電子スチルカメラなどが普及し、その電源として、ニッ
ケル・カドミウム電池、ニッケル・水素電池、リチウム
イオン電池などの二次電池が広く使用されるようになっ
てきた。
2. Description of the Related Art In recent years, the development of portable electronic devices has been remarkable. For example, telephones, notebook computers, camera-integrated VTRs,
Electronic still cameras and the like have become widespread, and secondary batteries such as nickel-cadmium batteries, nickel-metal hydride batteries, and lithium-ion batteries have been widely used as power sources.

【0003】とりわけ、リチウムイオン電池は、エネル
ギー密度、作動電圧が大きく、充放電を伴うサイクル寿
命特性に優れていることが注目されている。このリチウ
ムイオン電池の構造は、一般に、正極集電体、例えば2
0μm程度の厚さを持つアルミニウム箔の両面に、正極
活物質、例えば、LiCoO2の粉末をバインダーと非
水溶媒で混練し、ペースト状にしたものを塗布し、乾
燥、圧着一体化させた正極と、負極集電体、例えば10
μm程度の厚さを持つ銅箔を使用して、負極活物質、例
えば炭素粉末を正極と同様にバインダーと非水溶媒で混
練してペースト状にしたものを塗布し、乾燥、圧着一体
化させた負極とからなり、この正極と負極との両極の間
に絶縁性を有する多孔質セパレータを介して、順次重ね
合わせ、円筒形に巻き上げられている。更にこの両極が
円筒缶に収納され、非水電解液が注入され、スイッチ素
子、安全弁、端子などの部材を設けて二次電池として組
み立てられている。
[0003] In particular, lithium ion batteries have attracted attention because of their high energy density and operating voltage, and excellent cycle life characteristics involving charge and discharge. The structure of this lithium ion battery generally has a positive electrode current collector, for example, 2
A positive electrode obtained by kneading a paste of a positive electrode active material, for example, LiCoO 2 powder with a binder and a non-aqueous solvent on both sides of an aluminum foil having a thickness of about 0 μm, drying, pressing and integrating the mixture. And a negative electrode current collector, for example, 10
Using a copper foil having a thickness of about μm, a negative electrode active material, for example, a carbon powder kneaded with a binder and a non-aqueous solvent in the same manner as the positive electrode to form a paste is applied, dried, pressed and integrated. A negative electrode, which is successively overlapped and wound up into a cylindrical shape between the two electrodes of the positive electrode and the negative electrode via an insulating porous separator. Further, both electrodes are housed in a cylindrical can, a non-aqueous electrolyte is injected, and members such as a switch element, a safety valve, and a terminal are provided to assemble a secondary battery.

【0004】前記するように負極集電体には、導電性に
優れる金属箔、例えば、銅箔が多用されている。銅箔に
は製法の異なる圧延銅箔、電解銅箔が知られている。電
解銅箔は、圧延銅箔に比べて量産性に優れ、比較的製造
コストも安価である利点から、圧延銅箔と同様に二次電
池の負極集電体材料として使用されるようになってき
た。
As described above, a metal foil having excellent conductivity, for example, a copper foil, is often used for the negative electrode current collector. Rolled copper foils and electrolytic copper foils with different production methods are known as copper foils. Electrodeposited copper foil has been used as a negative electrode current collector material for secondary batteries in the same manner as rolled copper foil because of its advantages of superior mass productivity and relatively low manufacturing cost compared to rolled copper foil. Was.

【0005】電解銅箔は、一般に、硫酸−硫酸銅水溶液
を電解液として用い、一定速度で回転する円筒型陰極
と、これと対向配置させて設けた陽極との間に前記電解
液を供給し、通電しながら回転する陰極面に銅を析出さ
せ、所定厚みとなった銅箔を陰極面上から剥がしとり製
造される。
In general, an electrolytic copper foil is formed by using a sulfuric acid-copper sulfate aqueous solution as an electrolytic solution, and supplying the electrolytic solution between a cylindrical cathode rotating at a constant speed and an anode provided to face the same. Then, copper is deposited on the rotating cathode surface while energizing, and the copper foil having a predetermined thickness is peeled off from the cathode surface to manufacture the cathode foil.

【0006】この電解銅箔の機械的、物理的特性は、当
然のことながら、電解液の組成、必要に応じて加えられ
る各種の薬剤(添加剤)、また、電流密度、電解液供給
量などの電解条件に依存し、添加剤を適量添加すること
により、引張り強さ、伸び率が制御できることは知られ
ている。
The mechanical and physical properties of the electrolytic copper foil naturally include the composition of the electrolytic solution, various chemicals (additives) added as necessary, the current density, the supply amount of the electrolytic solution, and the like. It is known that the tensile strength and the elongation can be controlled by adding an appropriate amount of an additive depending on the electrolysis conditions.

【0007】ところで、二次電池に強く要請される特性
の一つとして、安全性の点から過充電が行われる際、集
電体(銅箔)が経時的に劣化し、亀裂を生じたりあるい
は破断するなどの不具合が生じないことが必要である。
しかしながら、従来の電解銅箔では、過充電後の集電体
(銅箔)の破断状態を表す過充電試験特性を十分に満足
させることはできなかった。
One of the characteristics strongly required of a secondary battery is that, when overcharging is performed from the viewpoint of safety, the current collector (copper foil) deteriorates with time, causing cracks or the like. It is necessary that failure such as breakage does not occur.
However, the conventional electrolytic copper foil could not sufficiently satisfy the overcharge test characteristics indicating the rupture state of the current collector (copper foil) after overcharge.

【0008】[0008]

【発明が解決しようとする課題】本発明の目的は、二次
電池用の集電体として好適に用いられる常温及び加熱後
の引張り強さに優れ、かつ常温及び加熱後の伸び率に優
れた電解銅箔を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide an excellent tensile strength at room temperature and after heating which is suitably used as a current collector for a secondary battery, and an excellent elongation at room temperature and after heating. An object of the present invention is to provide an electrolytic copper foil.

【0009】本発明の他の目的は、二次電池の集電体と
して用いた場合、過充電試験特性に優れた二次電池が得
られる二次電池の集電体用銅箔を提供することにある。
Another object of the present invention is to provide a current collector copper foil for a secondary battery which, when used as a current collector for a secondary battery, can provide a secondary battery having excellent overcharge test characteristics. It is in.

【0010】本発明の他の目的は、過充電試験特性に優
れた二次電池を提供することにある。
Another object of the present invention is to provide a secondary battery having excellent overcharge test characteristics.

【0011】[0011]

【課題を解決するための手段】すなわち、本発明は、銅
箔中の炭素含有量が5ppm以下であり、かつ硫黄含有
量が3ppm以下であることを特徴とする電解銅箔に関
する。
That is, the present invention relates to an electrolytic copper foil characterized in that the carbon content in the copper foil is 5 ppm or less and the sulfur content is 3 ppm or less.

【0012】本発明はまた、上記の電解銅箔からなるこ
とを特徴とする二次電池の集電体用銅箔に関する。
The present invention also relates to a current collector copper foil for a secondary battery, comprising the above-mentioned electrolytic copper foil.

【0013】本発明はまた、平面状集電体の表面に電極
構成物質層が形成されてなる正極及び負極を備える二次
電池において、正極及び負極の平面状集電体の少なくと
も一方が上記の電解銅箔であることを特徴とする二次電
池に関する。
[0013] The present invention also provides a secondary battery comprising a positive electrode and a negative electrode in which an electrode constituent material layer is formed on the surface of a planar current collector, wherein at least one of the positive and negative electrode planar current collectors is as described above. The present invention relates to a secondary battery characterized by being an electrolytic copper foil.

【0014】[0014]

【発明の実施の形態】本発明の電解銅箔は、銅箔中の炭
素含有量が5ppm以下であり、かつ硫黄含有量が3p
pm以下であることを特徴とする。このように銅箔中の
炭素含有量及び硫黄含有量を制御することにより、常温
及び加熱後の引張り強さに優れ、かつ常温及び加熱後の
伸び率に優れた電解銅箔が得られる。銅箔中の炭素含有
量が5ppmを超えると加熱後における伸び率が低下す
る。また、硫黄含有量が3ppmを超えると加熱後の伸
び率が低下する。炭素含有量の好ましい範囲は0.1〜
4ppmであり、硫黄含有量の好ましい範囲は0.1〜
2ppmである。
BEST MODE FOR CARRYING OUT THE INVENTION The electrolytic copper foil of the present invention has a carbon content of 5 ppm or less and a sulfur content of 3 ppm.
pm or less. By controlling the carbon content and the sulfur content in the copper foil in this way, an electrolytic copper foil having excellent tensile strength at normal temperature and after heating and excellent elongation at normal temperature and after heating can be obtained. When the carbon content in the copper foil exceeds 5 ppm, the elongation after heating decreases. On the other hand, if the sulfur content exceeds 3 ppm, the elongation after heating decreases. The preferred range of the carbon content is 0.1 to
4 ppm, and a preferable range of the sulfur content is 0.1 to
2 ppm.

【0015】さらに、本発明の電解銅箔は、銅箔中の酸
素含有量が5ppm以下であり、かつ窒素含有量が0.
5ppm以下であることが好ましい。銅箔中の酸素含有
量が5ppmを超えると加熱後の伸び率が低下する傾向
にあり、窒素含有量が0.5ppmを超えると加熱後の
伸び率が低下する傾向がある。酸素含有量のより好まし
い範囲は0.1〜4ppmであり、窒素含有量のより好
ましい範囲は0.1〜0.4ppmである。
Further, the electrolytic copper foil of the present invention has an oxygen content of 5 ppm or less in the copper foil and a nitrogen content of 0.1 ppm.
It is preferably at most 5 ppm. If the oxygen content in the copper foil exceeds 5 ppm, the elongation after heating tends to decrease, and if the nitrogen content exceeds 0.5 ppm, the elongation after heating tends to decrease. A more preferable range of the oxygen content is 0.1 to 4 ppm, and a more preferable range of the nitrogen content is 0.1 to 0.4 ppm.

【0016】さらに、本発明の電解銅箔は、銅箔中の炭
素、硫黄、酸素、窒素及び水素の合計含有量が15pp
m以下であることが好ましい。この不純物の合計量が1
5ppmを超えると常温における引張り強さ及び加熱後
の伸び率が低下する傾向がある。炭素、硫黄、酸素、窒
素及び水素の合計含有量は10ppm以下であることが
更に好ましい。
Further, in the electrolytic copper foil of the present invention, the total content of carbon, sulfur, oxygen, nitrogen and hydrogen in the copper foil is 15 pp.
m or less. The total amount of this impurity is 1
If it exceeds 5 ppm, the tensile strength at room temperature and the elongation after heating tend to decrease. More preferably, the total content of carbon, sulfur, oxygen, nitrogen and hydrogen is 10 ppm or less.

【0017】本発明において、炭素、硫黄、酸素、窒素
及び水素の測定は元素分析装置により行われる。炭素及
び硫黄の含有量の測定は、堀場製作所製EMIA−82
0により行なうことができ、酸素及び窒素の含有量の測
定は、堀場製作所製EMGA−620により行なうこと
ができ、水素の含有量の測定は、堀場製作所製EMGA
−521により行なうことができる。
In the present invention, the measurement of carbon, sulfur, oxygen, nitrogen and hydrogen is performed by an elemental analyzer. The measurement of the content of carbon and sulfur was performed using EMIA-82 manufactured by Horiba, Ltd.
0, the content of oxygen and nitrogen can be measured by EMGA-620 manufactured by Horiba, and the content of hydrogen can be measured by EMGA manufactured by Horiba, Ltd.
-521.

【0018】上記のように不純物含有量が制御された本
発明の銅箔は、例えば、電解銅箔製造に用いられる電解
液として有機系不純物を高度に除去したものを用いて電
解処理することにより得られる。
The copper foil of the present invention, in which the content of impurities is controlled as described above, can be obtained, for example, by subjecting the copper foil of the present invention to electrolytic treatment using, as an electrolytic solution used in the production of electrolytic copper foil, a highly-removed organic impurity. can get.

【0019】電解液中の不純物を高度に除去する方法と
しては、電解液製造に用いられる原料である銅線を60
0〜900℃で30〜60分間焼成して用いる方法、硫
酸などを用いて銅線を洗浄する方法、高純度の銅線材、
硫酸銅、硫酸を用いる方法、電解液中に通常使用される
各種添加剤、例えばチオ尿素、アラビアゴム、ゼラチ
ン、膠などを使用しない方法、使用する水として蒸留水
又は純水を使用する方法など、あるいはこれらを適宜組
み合わせる方法等が挙げられる。
As a method for removing impurities in the electrolytic solution to a high degree, a copper wire, which is a raw material used for producing the electrolytic solution, is used for a 60-degree process.
A method of firing at 0 to 900 ° C. for 30 to 60 minutes, a method of cleaning a copper wire using sulfuric acid or the like, a high-purity copper wire,
A method using copper sulfate or sulfuric acid, a method not using thiourea, gum arabic, gelatin, glue, etc. commonly used in an electrolytic solution, a method using distilled water or pure water as water to be used, etc. Or a method of appropriately combining them.

【0020】その他に、電解液を活性炭ろ過装置により
処理したり、オゾン発生装置により液中に存在する有機
物を酸化分解したりして、電解液中の不純物を除去する
方法等が挙げられる。
In addition, a method of removing impurities in the electrolyte by treating the electrolyte with an activated carbon filter or oxidizing and decomposing organic substances present in the solution with an ozone generator can be used.

【0021】上記の方法により得られた不純物が高度に
除去された電解液を用いて電解銅箔を製造することによ
り、所定の元素含有量の電解銅箔が得られる。
By producing an electrolytic copper foil using the electrolytic solution obtained by the above-mentioned method from which impurities are highly removed, an electrolytic copper foil having a predetermined element content can be obtained.

【0022】本発明の電解銅箔は、銅箔中の炭素含有量
及び硫黄含有量が前記範囲内にあり、常温及び加熱後の
引張り強さに優れ、かつ常温及び加熱後の伸び率に優
れ、二次電池の集電体として好適に用いられる。
The electrodeposited copper foil of the present invention has the carbon content and the sulfur content in the copper foil within the above-mentioned ranges, has excellent tensile strength at room temperature and after heating, and has excellent elongation at room temperature and after heating. And a current collector of a secondary battery.

【0023】本発明の電解銅箔の表面には必要に応じ
て、粗面化処理層や、防錆のためにクロメート処理層な
どの防錆層が設けられていてもよい。
The surface of the electrolytic copper foil of the present invention may be provided with a rust-preventing layer such as a roughening-treated layer or a chromate-treated layer for rust prevention, if necessary.

【0024】本発明の二次電池は、平面状集電体の表面
に電極構成物質層が形成されてなる正極及び負極を備え
たものであり、本発明の電解銅箔を正極及び負極の集電
体の少なくとも一方、好ましくは負極集電体として使用
している。このように、本発明の電解銅箔を集電体とし
て用いることにより、過充電試験特性に優れた二次電池
が得られる。その理由は、本発明の電解銅箔は、従来の
電解銅箔と比べて、加熱後の銅箔の強度を表す引き裂き
伝播時間が長く、二次電池の過充電試験の箔破れが起こ
りにくくなるからである。
The secondary battery of the present invention includes a positive electrode and a negative electrode each having a planar current collector and an electrode constituting material layer formed on the surface thereof. It is used as at least one of the current collectors, preferably as a negative electrode current collector. Thus, by using the electrolytic copper foil of the present invention as a current collector, a secondary battery having excellent overcharge test characteristics can be obtained. The reason is that the electrolytic copper foil of the present invention has a longer tear propagation time indicating the strength of the copper foil after heating as compared with the conventional electrolytic copper foil, and the foil tear of the overcharge test of the secondary battery is less likely to occur. Because.

【0025】本発明の二次電池の負極の電極構成物質と
しては、熱分解炭素類、コークス類、グラファイト類、
金属リチウム、リチウム合金、ポリアセチレン、ポリピ
ロールなどを使用することができる。
The electrode constituting materials of the negative electrode of the secondary battery of the present invention include pyrolytic carbons, cokes, graphites, and the like.
Metallic lithium, lithium alloy, polyacetylene, polypyrrole, and the like can be used.

【0026】本発明の二次電池の正極の電極構成物質と
しては、特に制限はなく、LiNiO2、LiCoO2
LiMn24等を単独、又は混合して使用することがで
きる。
The material constituting the positive electrode of the positive electrode of the secondary battery of the present invention is not particularly limited, and may be LiNiO 2 , LiCoO 2 ,
LiMn 2 O 4 or the like can be used alone or as a mixture.

【0027】電解液としては、LiClO4、LiPF6
等のリチウム塩を、例えば炭酸エチレン、炭酸ジメチル
などの非水系溶剤に溶解したいわゆる有機系電解液をポ
リフッ化ビニリデン等の高分子固体電解質に含ませた電
解液などを使用することができる。
As the electrolyte, LiClO 4 , LiPF 6
For example, an electrolyte in which a so-called organic electrolyte obtained by dissolving a lithium salt such as in a non-aqueous solvent such as ethylene carbonate or dimethyl carbonate in a polymer solid electrolyte such as polyvinylidene fluoride can be used.

【0028】セパレータとしては、例えばポリエチレ
ン、ポリプロピレン等のポリオレフィンを主成分とした
不織布、クロス、微孔フィルム又はこれらを組み合わせ
たものを使用することができる。
As the separator, for example, a nonwoven fabric, cloth, microporous film, or a combination thereof, containing a polyolefin such as polyethylene or polypropylene as a main component can be used.

【0029】なお、円筒型リチウムイオン電池の一例の
一部断面正面図を図1に示す。
FIG. 1 shows a partial cross-sectional front view of an example of a cylindrical lithium ion battery.

【0030】[0030]

【実施例】以下、本発明の実施例及びその比較例によっ
て本発明を更に具体的に説明するが、本発明はこれらの
実施例に限定されるものではない。
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to Examples of the present invention and Comparative Examples thereof, but the present invention is not limited to these Examples.

【0031】実施例1 (1)電解銅箔の製造 銅原料である市販の銅線を700℃で1時間焼成し、更
に100g/l 硫酸水溶液を用いて20分間酸洗処理
し、銅線に付着する不純物を除去した。次いでこの焼成
処理及び酸洗処理された銅線を硫酸に溶解し、硫酸銅溶
液を得た。この硫酸銅溶液を活性炭を用いたろ過装置に
よりろ過して下記組成の電解液を得た。なお、硫酸とし
ては精製硫酸を使用した。 硫酸銅(CuSO4・5H2O) 280g/l 硫酸(H2SO4) 80g/l この電解液を用いて、貴金属酸化物被覆チタンを陽極、
チタン製回転ドラムを陰極として、電流密度50A/d
2、液温50℃の条件で電解することによって、厚さ
10μmの電解銅箔を製造した。得られた銅箔をサンプ
ルとして銅箔中の不純物量の測定及び下記の特性試験を
行い、その結果を表1に示す。 (a)引張り強さ 常温(23℃)及び130℃で15時間加熱後の引張り
強さをJIS C 6511に基づいて測定した。 (b)伸び率 常温(23℃)及び130℃で15時間加熱後の伸び率
をJIS C 6511に基づいて測定した。 (c)引き裂き伝播時間 130℃で15時間加熱後の引張り強さ試験(クロスヘ
ッドスピード2.0mm/分、チャートスピード200
mm/分)における箔の亀裂開始から破断完了までの時
間(秒)を測定した。
Example 1 (1) Production of Electrodeposited Copper Foil A commercially available copper wire as a copper raw material was baked at 700 ° C. for 1 hour, and further subjected to an acid pickling treatment with a 100 g / l sulfuric acid aqueous solution for 20 minutes. Adhering impurities were removed. Next, the calcined and pickled copper wire was dissolved in sulfuric acid to obtain a copper sulfate solution. The copper sulfate solution was filtered by a filtration device using activated carbon to obtain an electrolyte having the following composition. Note that purified sulfuric acid was used as the sulfuric acid. Copper sulfate (CuSO 4 .5H 2 O) 280 g / l Sulfuric acid (H 2 SO 4 ) 80 g / l Using this electrolytic solution, a noble metal oxide-coated titanium was used as an anode,
Current density of 50 A / d using titanium drum as cathode
Electrolysis was performed under the conditions of m 2 and a liquid temperature of 50 ° C. to produce an electrolytic copper foil having a thickness of 10 μm. Using the obtained copper foil as a sample, the amount of impurities in the copper foil was measured and the following characteristic tests were performed. The results are shown in Table 1. (A) Tensile strength Tensile strength after heating at room temperature (23 ° C.) and 130 ° C. for 15 hours was measured based on JIS C 6511. (B) Elongation The elongation after heating at room temperature (23 ° C.) and 130 ° C. for 15 hours was measured based on JIS C 6511. (C) Tear propagation time Tensile strength test after heating at 130 ° C. for 15 hours (crosshead speed 2.0 mm / min, chart speed 200
mm / min), the time (sec) from the start of the cracking of the foil to the completion of the fracture was measured.

【0032】(2)リチウムイオン電池の製造 図1は、円筒形リチウムイオン電池の一部断面正面図を
示し、1は正極、2は負極、3はセパレータ、4は正極
リード、5は負極リード、6は正極蓋、7は電池缶及び
8はガスケットである。
(2) Manufacture of Lithium Ion Battery FIG. 1 shows a partial cross-sectional front view of a cylindrical lithium ion battery, wherein 1 is a positive electrode, 2 is a negative electrode, 3 is a separator, 4 is a positive electrode lead, and 5 is a negative electrode lead. , 6 is a positive electrode cover, 7 is a battery can, and 8 is a gasket.

【0033】図1に示すリチウムイオン電池は以下のよ
うにして作製した。正極活物質としては、LiCoO2
を90重量部、導電助剤として平均粒径が1μmの黒鉛
を5重量部、及び結着剤としてポリフッ化ビニリデン
(PVDF)を5重量部添加して、これにN−メチル−
2−ピロリドンを5重量部加え正極用合剤ペーストを調
製した。同様に負極活物質としてピッチ系炭素繊維90
重量部及び結着剤としてPVDFを10重量部添加し
て、これにN−メチル−2−ピロリドンを10重量部混
合して負極用合剤ペーストを得た。
The lithium ion battery shown in FIG. 1 was manufactured as follows. As the positive electrode active material, LiCoO 2
90 parts by weight, 5 parts by weight of graphite having an average particle size of 1 μm as a conductive aid, and 5 parts by weight of polyvinylidene fluoride (PVDF) as a binder.
5 parts by weight of 2-pyrrolidone was added to prepare a positive electrode mixture paste. Similarly, pitch-based carbon fiber 90 is used as a negative electrode active material.
10 parts by weight of PVDF as a binder and 10 parts by weight of N-methyl-2-pyrrolidone were mixed with the mixture to obtain a negative electrode mixture paste.

【0034】次に正極用合剤ペーストを厚みが20μm
のアルミニウム箔の両面に塗布し、120℃で10分間
予備乾燥し、ローラープレスによって電極を加圧成形し
た後130℃で15時間真空乾燥し、厚みを160μm
とした。単位面積当たりの正極合剤(ペーストから溶剤
を除いたもの)塗布量は、25mg/cm2であり、幅
が54mmで長さが437mmの大きさに切り出して正
極1を作製した。但し正極1の両端の長さ10mmは、
正極用合剤が塗布されておらず、アルミニウム箔が露出
されており、この一方に正極リード4を、超音波接合に
よって圧着した。
Next, the mixture paste for the positive electrode was
And pre-dried at 120 ° C. for 10 minutes, pressure-formed the electrode by a roller press, and vacuum-dried at 130 ° C. for 15 hours to a thickness of 160 μm.
And The coated amount of the positive electrode mixture (excluding the solvent from the paste) per unit area was 25 mg / cm 2 , and was cut into a size of 54 mm in width and 437 mm in length to prepare a positive electrode 1. However, the length 10 mm of both ends of the positive electrode 1 is
The positive electrode mixture was not applied and the aluminum foil was exposed, and the positive electrode lead 4 was pressure-bonded to one of the aluminum foil by ultrasonic bonding.

【0035】一方負極用合剤ペーストを、厚みが10μ
mの実施例1で得た銅箔の両面に塗布し、その後120
℃で10分間予備乾燥し、ローラープレスによって電極
を加圧成形した後130℃で15時間真空乾燥し、厚み
を200μmとした。単位面積当たりの負極用合剤(ペ
ーストから溶剤を除いたもの)の塗布量は、13mg/
cm2であり、幅が56mmで長さが480mmの大き
さに切り出して、負極2を作製した。これを正極1と同
様に、負極2の長さ10mmの部分は、負極用合剤が塗
布されておらず、銅箔が露出しており、この一方に負極
リード5を超音波接合により圧着した。
On the other hand, the negative electrode mixture paste was
m on both sides of the copper foil obtained in Example 1,
After pre-drying at 10 ° C. for 10 minutes, the electrode was pressure-formed by a roller press, and then vacuum-dried at 130 ° C. for 15 hours to a thickness of 200 μm. The applied amount of the negative electrode mixture (paste excluding the solvent) per unit area was 13 mg /
Negative electrode 2 was prepared by cutting out into a size of cm 2 , 56 mm in width and 480 mm in length. As in the case of the positive electrode 1, the negative electrode 2 was not coated with the mixture for the negative electrode and the copper foil was exposed in the portion having a length of 10 mm, and the negative electrode lead 5 was pressure-bonded to one of the two parts by ultrasonic bonding. .

【0036】セパレータ3は、厚みが25μm、幅が5
8mmのポリエチレン製の微孔膜を用いた。次いで図1
に示すように正極1、セパレータ3、負極2及びセパレ
ータ3の順で重ね合わせ、これを捲回して電極群とし
た。これを電池缶に挿入して、負極リード5を缶底に溶
接し、正極蓋6を加締るための絞り部を設けた。この後
体積比で1:1の炭酸エチレンと炭酸ジメチルの混合溶
媒に六フッ化リン酸リチウムを1モル/リットルで溶解
させた電解液を電池缶7に注入した後、正極リード4を
正極蓋6に溶接した後、正極蓋6をとりつけてリチウム
イオン電池を得た。
The separator 3 has a thickness of 25 μm and a width of 5 μm.
An 8 mm polyethylene microporous membrane was used. Then Figure 1
As shown in (1), the positive electrode 1, the separator 3, the negative electrode 2, and the separator 3 were superimposed in this order, and were wound to form an electrode group. This was inserted into a battery can, the negative electrode lead 5 was welded to the bottom of the can, and a throttle portion for caulking the positive electrode lid 6 was provided. Thereafter, an electrolyte obtained by dissolving lithium hexafluorophosphate in a mixed solvent of ethylene carbonate and dimethyl carbonate at a volume ratio of 1: 1 at 1 mol / liter is poured into the battery can 7, and then the positive electrode lead 4 is connected to the positive electrode cover. After welding to 6, a positive electrode lid 6 was attached to obtain a lithium ion battery.

【0037】過充電試験 得られたリチウムイオン電池を用いて、直流2Aで40
分間及び直流3Aで30分間の過充電後、それぞれ電池
を解体し、負極銅箔の巻き終わり箇所(5cm×5c
m、25cm2)を目視観察し銅箔破れの有無を調べそ
の個数を測定した。その結果を表1に示す。
Overcharge test Using the obtained lithium-ion battery, 40
After overcharging for 30 minutes at 3 A and DC for 3 minutes, the batteries were disassembled, and the winding end point of the negative electrode copper foil (5 cm × 5 c
m, 25 cm 2 ) was visually observed to determine whether or not the copper foil was broken, and the number thereof was measured. Table 1 shows the results.

【0038】実施例2 電解銅箔の製造において、硫酸銅溶液(電解液)を作製
するにあたり、銅線の焼成処理を行わなかった以外は、
実施例1と同様にして電解銅箔を製造した。この銅箔を
用いて、実施例1と同様に銅箔中の不純物量の測定及び
(a)引張り強さ、(b)伸び率、(c)引き裂き伝播
時間の各特性試験を行い、その結果を表1に示した。ま
た、この銅箔を用いて実施例1と同様にしてリチウムイ
オン電池を製造し、実施例1と同様に過充電試験を行い
その結果を表1に示した。
Example 2 In the production of an electrolytic copper foil, a copper sulfate solution (electrolytic solution) was prepared except that the copper wire was not fired.
An electrolytic copper foil was manufactured in the same manner as in Example 1. Using this copper foil, measurement of the amount of impurities in the copper foil and each characteristic test of (a) tensile strength, (b) elongation, and (c) tear propagation time were performed in the same manner as in Example 1. As a result, Are shown in Table 1. Further, a lithium ion battery was manufactured using this copper foil in the same manner as in Example 1, and an overcharge test was performed in the same manner as in Example 1. The results are shown in Table 1.

【0039】実施例3 電解銅箔の製造において、硫酸銅溶液(電解液)を作製
するにあたり、銅線の酸洗処理を行わなかった以外は、
実施例1と同様にして電解銅箔を製造した。この銅箔を
用いて、実施例1と同様に銅箔中の不純物量の測定及び
(a)引張り強さ、(b)伸び率、(c)引き裂き伝播
時間の各特性試験を行い、その結果を表1に示した。ま
た、この銅箔を用いて実施例1と同様にしてリチウムイ
オン電池を製造し、実施例1と同様に過充電試験を行い
その結果を表1に示した。
Example 3 In the production of the electrolytic copper foil, except that the pickling treatment of the copper wire was not performed in preparing the copper sulfate solution (electrolytic solution).
An electrolytic copper foil was manufactured in the same manner as in Example 1. Using this copper foil, measurement of the amount of impurities in the copper foil and each characteristic test of (a) tensile strength, (b) elongation, and (c) tear propagation time were performed in the same manner as in Example 1. As a result, Are shown in Table 1. Further, a lithium ion battery was manufactured using this copper foil in the same manner as in Example 1, and an overcharge test was performed in the same manner as in Example 1. The results are shown in Table 1.

【0040】比較例1 電解銅箔の製造において、硫酸銅溶液(電解液)を作製
するにあたり、銅線に焼成処理及び酸洗処理を行わなか
ったこと、及び電解液にゼラチンを0.5ppm含有さ
せたこと以外は、実施例1と同様にして電解銅箔を製造
した。この銅箔を用いて、実施例1と同様に銅箔中の不
純物量の測定及び(a)引張り強さ、(b)伸び率、
(c)引き裂き伝播時間の各特性試験を行い、その結果
を表1に示した。また、この銅箔を用いて実施例1と同
様にしてリチウムイオン電池を製造し、実施例1と同様
に過充電試験を行いその結果を表1に示した。
Comparative Example 1 In the production of an electrolytic copper foil, in preparing a copper sulfate solution (electrolytic solution), no baking treatment and no pickling treatment were performed on the copper wire, and 0.5 ppm of gelatin was contained in the electrolytic solution. Except having made it, it carried out similarly to Example 1, and manufactured the electrolytic copper foil. Using this copper foil, measurement of the amount of impurities in the copper foil and (a) tensile strength, (b) elongation,
(C) Each property test of the tear propagation time was performed, and the results are shown in Table 1. Further, a lithium ion battery was manufactured using this copper foil in the same manner as in Example 1, and an overcharge test was performed in the same manner as in Example 1. The results are shown in Table 1.

【0041】比較例2 電解銅箔の製造において、硫酸銅溶液(電解液)を作製
するにあたり、電解液にゼラチンを3ppm、塩素イオ
ンを20ppm含有させたこと以外は、実施例1と同様
にして電解銅箔を製造した。この銅箔を用いて、実施例
1と同様に銅箔中の不純物量の測定及び(a)引張り強
さ、(b)伸び率、(c)引き裂き伝播時間の各特性試
験を行い、その結果を表1に示した。また、この銅箔を
用いて実施例1と同様にしてリチウムイオン電池を製造
し、実施例1と同様に過充電試験を行いその結果を表1
に示した。
Comparative Example 2 In the production of an electrolytic copper foil, a copper sulfate solution (electrolytic solution) was prepared in the same manner as in Example 1 except that the electrolytic solution contained 3 ppm of gelatin and 20 ppm of chloride ions. An electrolytic copper foil was manufactured. Using this copper foil, measurement of the amount of impurities in the copper foil and each characteristic test of (a) tensile strength, (b) elongation, and (c) tear propagation time were performed in the same manner as in Example 1. As a result, Are shown in Table 1. Using this copper foil, a lithium ion battery was manufactured in the same manner as in Example 1, and an overcharge test was performed in the same manner as in Example 1. The results are shown in Table 1.
It was shown to.

【0042】比較例3 電解銅箔の製造において、硫酸銅溶液(電解液)を作製
するにあたり、電解液にゼラチンを10ppm含有させ
たこと以外は、実施例1と同様にして電解銅箔を製造し
た。この銅箔を用いて、実施例1と同様に銅箔中の不純
物量の測定及び(a)引張り強さ、(b)伸び率、
(c)引き裂き伝播時間の各特性試験を行い、その結果
を表1に示した。また、この銅箔を用いて実施例1と同
様にしてリチウムイオン電池を製造し、実施例1と同様
に過充電試験を行いその結果を表1に示した。
Comparative Example 3 An electrolytic copper foil was produced in the same manner as in Example 1 except that the electrolytic solution contained 10 ppm of gelatin in producing the copper sulfate solution (electrolytic solution). did. Using this copper foil, measurement of the amount of impurities in the copper foil and (a) tensile strength, (b) elongation,
(C) Each property test of the tear propagation time was performed, and the results are shown in Table 1. Further, a lithium ion battery was manufactured using this copper foil in the same manner as in Example 1, and an overcharge test was performed in the same manner as in Example 1. The results are shown in Table 1.

【0043】比較例4 市販の厚さ10μmの圧延銅箔[C1100(JIS
H 3110、タフピッチ銅)、Cu99.90%以
上]を用いて実施例1と同様にしてリチウムイオン電池
を製造し、実施例1と同様に評価試験を行いその結果を
表1に示した。
Comparative Example 4 A commercially available rolled copper foil having a thickness of 10 μm [C1100 (JIS)
H 3110, tough pitch copper) and Cu of 99.90% or more], a lithium ion battery was manufactured in the same manner as in Example 1, and an evaluation test was performed in the same manner as in Example 1. The results are shown in Table 1.

【0044】[0044]

【表1】 実施例1〜3において、本発明の電解銅箔は銅箔中の不
純物の合計量が15ppm以下に低減されているので、
銅箔特性の引張り強さ、伸び率を同時に高めている。特
に常温引張り強さが55kgf/mm2以上、加熱後伸
び率が25%以上を保持している。また、引き裂き伝播
時間が長く、かつ電池の過充電試験において破断防止に
優れている。
[Table 1] In Examples 1 to 3, the electrolytic copper foil of the present invention has the total amount of impurities in the copper foil reduced to 15 ppm or less.
The tensile strength and elongation of the copper foil properties are simultaneously increased. In particular, it has a room temperature tensile strength of 55 kgf / mm 2 or more and an elongation after heating of 25% or more. In addition, it has a long tear propagation time and is excellent in preventing breakage in a battery overcharge test.

【0045】一方、比較例1〜3においては、銅箔中の
不純物の合計量が15ppmを超えていることから常温
及び加熱後における引張り強さ、伸び率を本発明のよう
に高められず、二次電池としての過充電試験から明らか
なように、信頼性を欠くものである。また、比較例4
(圧延銅箔)では、特に加熱後の引張り強さ及び常温伸
び率が本発明の銅箔に比べて低い傾向を示し、過充電試
験の評価では本発明の銅箔を使用したものより若干劣っ
ていることが判った。
On the other hand, in Comparative Examples 1 to 3, since the total amount of impurities in the copper foil exceeded 15 ppm, the tensile strength and the elongation at room temperature and after heating could not be increased as in the present invention. As is clear from the overcharge test as a secondary battery, the battery lacks reliability. Comparative Example 4
In the case of (rolled copper foil), the tensile strength and room temperature elongation after heating tend to be lower than those of the copper foil of the present invention, and are slightly inferior to those using the copper foil of the present invention in the evaluation of the overcharge test. It turned out that.

【0046】[0046]

【発明の効果】本発明の電解銅箔は、常温及び加熱後の
引張り強さに優れ、かつ常温及び加熱後の伸び率に優
れ、二次電池用の集電体銅箔として好適に用いられる。
The electrolytic copper foil of the present invention has excellent tensile strength at room temperature and after heating, and has excellent elongation at room temperature and after heating, and is suitable for use as a current collector copper foil for secondary batteries. .

【0047】また、本発明の二次電池用の集電体銅箔を
用いると、過充電試験特性に優れた二次電池を得ること
ができる。
When the current collector copper foil for a secondary battery of the present invention is used, a secondary battery having excellent overcharge test characteristics can be obtained.

【0048】また、本発明の二次電池は、過充電試験特
性特性に優れたものである。
Further, the secondary battery of the present invention has excellent overcharge test characteristics.

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

【図1】円筒形リチウムイオン電池の一部断面正面図で
ある。
FIG. 1 is a partial cross-sectional front view of a cylindrical lithium ion battery.

【符号の説明】[Explanation of symbols]

1 正極 2 負極 3 セパレータ 4 正極リード 5 負極リード 6 正極蓋 7 電池缶 8 ガスケット Reference Signs List 1 positive electrode 2 negative electrode 3 separator 4 positive electrode lead 5 negative electrode lead 6 positive electrode cover 7 battery can 8 gasket

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小林 勝己 茨城県下館市下江連1226番地 日本電解株 式会社下館工場内 (72)発明者 阿曽 和義 茨城県下館市下江連1226番地 日本電解株 式会社下館工場内 Fターム(参考) 5H017 AA03 AS10 CC01 EE01 EE08 HH01 5H028 AA01 CC20 EE01 HH01 5H029 AJ02 AK03 AK19 AL06 AL12 AL16 AM01 AM03 AM05 AM07 AM16 BJ02 BJ14 DJ07 EJ01 HJ01  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Katsumi Kobayashi 1226 Shimoedashiri, Shimodate City, Ibaraki Pref. Inside the Shimodate Plant of Nihon Electrolysis Co., Ltd. F-term in Shimodate factory (reference) 5H017 AA03 AS10 CC01 EE01 EE08 HH01 5H028 AA01 CC20 EE01 HH01 5H029 AJ02 AK03 AK19 AL06 AL12 AL16 AM01 AM03 AM05 AM07 AM16 BJ02 BJ14 DJ07 EJ01 HJ01

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 銅箔中の炭素含有量が5ppm以下であ
り、かつ硫黄含有量が3ppm以下であることを特徴と
する電解銅箔。
1. An electrolytic copper foil characterized in that the carbon content in the copper foil is 5 ppm or less and the sulfur content is 3 ppm or less.
【請求項2】 銅箔中の酸素含有量が5ppm以下であ
り、かつ窒素含有量が0.5ppm以下である請求項1
記載の電解銅箔。
2. The copper foil has an oxygen content of 5 ppm or less and a nitrogen content of 0.5 ppm or less.
Electrolytic copper foil as described.
【請求項3】 銅箔中の炭素、硫黄、酸素、窒素及び水
素の合計含有量が15ppm以下である請求項1又は2
記載の電解銅箔。
3. The copper foil has a total content of carbon, sulfur, oxygen, nitrogen and hydrogen of 15 ppm or less.
Electrolytic copper foil as described.
【請求項4】 請求項1、2又は3記載の電解銅箔から
なることを特徴とする二次電池の集電体用銅箔。
4. A copper foil for a current collector of a secondary battery, comprising the electrolytic copper foil according to claim 1, 2 or 3.
【請求項5】 平面状集電体の表面に電極構成物質層が
形成されてなる正極及び負極を備える二次電池におい
て、正極及び負極の平面状集電体の少なくとも一方が請
求項1、2又は3記載の電解銅箔であることを特徴とす
る二次電池。
5. A secondary battery comprising a positive electrode and a negative electrode in which an electrode constituent material layer is formed on the surface of a flat current collector, wherein at least one of the positive and negative flat current collectors is provided. Or a secondary battery characterized by being the electrolytic copper foil according to 3.
JP35321398A 1998-12-11 1998-12-11 Electrolytic copper foil, copper foil for current collector of secondary battery and secondary battery Expired - Lifetime JP3850155B2 (en)

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TWI821472B (en) * 2018-12-10 2023-11-11 日商日本電解股份有限公司 Electrolytic copper foil and manufacturing method thereof
JP7450932B2 (en) 2018-12-10 2024-03-18 日本電解株式会社 Electrolytic copper foil and its manufacturing method
US12091766B2 (en) 2018-12-10 2024-09-17 Nippon Denkai, Ltd. Electrolytic copper foil and method for producing same
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
WO2024116782A1 (en) * 2022-11-29 2024-06-06 パナソニックIpマネジメント株式会社 Lithium secondary battery

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