JPH09180725A - Binder solution for battery and electrode mix - Google Patents

Binder solution for battery and electrode mix

Info

Publication number
JPH09180725A
JPH09180725A JP7350782A JP35078295A JPH09180725A JP H09180725 A JPH09180725 A JP H09180725A JP 7350782 A JP7350782 A JP 7350782A JP 35078295 A JP35078295 A JP 35078295A JP H09180725 A JPH09180725 A JP H09180725A
Authority
JP
Japan
Prior art keywords
acid
polymer
vinylidene fluoride
binder solution
organic solvent
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
JP7350782A
Other languages
Japanese (ja)
Other versions
JP3540080B2 (en
Inventor
Hidetora Kashio
秀虎 樫尾
Katsuo Horie
勝雄 堀江
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.)
Kureha Corp
Original Assignee
Kureha Corp
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 Kureha Corp filed Critical Kureha Corp
Priority to JP35078295A priority Critical patent/JP3540080B2/en
Priority to US08/779,955 priority patent/US6200703B1/en
Priority to EP96309481A priority patent/EP0782208B1/en
Priority to CA002193935A priority patent/CA2193935C/en
Priority to DE69635888T priority patent/DE69635888T8/en
Priority to KR1019960072262A priority patent/KR100263735B1/en
Publication of JPH09180725A publication Critical patent/JPH09180725A/en
Application granted granted Critical
Publication of JP3540080B2 publication Critical patent/JP3540080B2/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

Landscapes

  • Battery Electrode And Active Subsutance (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Paints Or Removers (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide binder solution, which can form a stable battery electrode, by dissolving vinylidene fluorite polymer in the organic solvent, and sampling a part thereof, and adding acid so as to adjust the pH of the liquid, which is obtained by diluting the sampled solvent with ion exchanged water. SOLUTION: At the time of obtaining the vinylidene fluorite polymer binder solution, vinylidene fluorite polymer at about 0.1-20 parts by weight in relation to the organic solvent at 100 parts by weight is dissolved in the organic solvent. A part of the solvent is sampled, and pH is adjusted by adding the acid so that the pH of the liquid, which is obtained by diluting the sampled solvent with the ion exchanged water at 10 times, becomes 9 or less. As the acid to be added, organic acid such as acrylic acid, formic acid and citric acid is desirable. Powder electrode material is dispersed for mixing in the vinylidene fluorite polymer binder solution so as to obtain the electrode mix. Single polymer, co-polymer and the denaturated material of vinylidene fluorite is contained in the vinylidene fluorite group polymer. As the organic solvent, the nitrogen contained organic solvent is desirable.

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、非水系電池、特に
リチウムイオン電池、の粉末電極材料(主として電極活
物質および必要に応じて加えられる導電性助剤)を電極
に安定的に固着させるために用いられるフッ化ビニリデ
ン系重合体からなるバインダーの溶液、すなわちフッ化
ビニリデン系重合体バインダー溶液、およびこれに粉末
電極材料を分散させてなる電極合剤に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is intended to stably fix a powder electrode material (mainly an electrode active material and a conductive auxiliary agent added as necessary) of a non-aqueous battery, particularly a lithium ion battery, to an electrode. The present invention relates to a solution of a binder made of a vinylidene fluoride-based polymer, that is, a vinylidene fluoride-based polymer binder solution, and an electrode mixture prepared by dispersing a powder electrode material therein.

【0002】[0002]

【従来の技術】近年電子技術の発展はめざましく、各種
の機器が小型軽量化されてきている。この電子機器の小
型軽量化と相まって、その電源となる電池の小型軽量化
の要望も非常に大きくなってきている。少ない容積及び
重量でより大きなエネルギーを得るためには電池一本当
たりの電圧が高いことが必要となり、この見地から最近
リチウムまたはリチウムイオンを吸蔵可能な炭素質材料
を負極活物質とし、正極活物質として例えばリチウムコ
バルト酸化物を使用した非水系電解液を用いる電池が注
目されている。
2. Description of the Related Art In recent years, the development of electronic technology has been remarkable, and various devices have been reduced in size and weight. Along with the miniaturization and weight reduction of this electronic device, the demand for the miniaturization and weight reduction of a battery serving as a power source for the electronic device has also become very large. In order to obtain more energy with a small volume and weight, it is necessary to increase the voltage per battery. From this viewpoint, recently, a carbonaceous material capable of storing lithium or lithium ions is used as a negative electrode active material, and a positive electrode active material is used. For example, a battery using a non-aqueous electrolyte using lithium cobalt oxide has attracted attention.

【0003】しかしながら、このような非水系電池にお
いては、水系の電解液のイオン伝導度が通常10-1S/
cmであるのに対し、非水系電解液のイオン伝導度は1
-2〜10-4S/cm程度と低いため、実用電池として
は厚さ数μmから数百μmと薄く且つ大面積の電極を用
いることが必須となってきている。かかる薄膜で且つ大
面積の電極を工業的に安価に得る方法としては、電極活
物質のバインダーとなる有機重合体を溶媒に溶解してな
るバインダー溶液中に、粉末電極材料を分散させた後、
金属電極箔または金属網上に塗布乾燥して電極を成型す
る方法が知られている。また、このような非水系電池用
のバインダー溶液としては、特開平6−93025や特
開平6−172452号各公報に記載されているよう
に、各種のフッ化ビニリデン系重合体を、N−メチル−
2−ピロリドン、ジメチルフォルムアミド、N,N−ジ
メチルアセトアミドなどの極性溶媒に溶解したものが知
られている。これは、フッ化ビニリデン系重合体が、耐
薬品性、耐候性、耐汚染性等に優れ、上記のような極性
溶媒には溶解するが、非水系電池に用いられる非水系電
解液に対しては、多少膨潤するものの安定であり、また
共重合あるいは変性処理等により金属等の基材に対して
も良好な接着性を保持し得るからである。
[0003] However, in such a non-aqueous battery, the ionic conductivity of the aqueous electrolyte is usually 10 -1 S / S.
cm, whereas the ionic conductivity of the non-aqueous electrolyte is 1
Since it is as low as about 0 −2 to 10 −4 S / cm, it is essential to use a thin and large-area electrode having a thickness of several μm to several hundred μm as a practical battery. Such a thin film and as a method of industrially inexpensively obtaining a large area electrode, as a binder solution obtained by dissolving an organic polymer serving as a binder of an electrode active material in a solvent, after dispersing the powder electrode material,
A method is known in which an electrode is molded by coating and drying it on a metal electrode foil or a metal net. Further, as such a binder solution for a non-aqueous battery, various vinylidene fluoride-based polymers may be used as N-methyl as described in JP-A-6-93025 and JP-A-6-172452. −
It is known to be dissolved in a polar solvent such as 2-pyrrolidone, dimethylformamide, N, N-dimethylacetamide. This is because the vinylidene fluoride polymer is excellent in chemical resistance, weather resistance, stain resistance and the like and dissolves in the polar solvent as described above, but with respect to the non-aqueous electrolyte solution used in the non-aqueous battery. The reason is that although it swells to some extent, it is stable, and good adhesiveness can be maintained even on a substrate such as a metal by copolymerization or modification treatment.

【0004】[0004]

【発明が解決しようとする課題】上述したようなフッ化
ビニリデン系重合体を、バインダーとして、これを極性
有機溶媒に溶解した際に、溶媒のロットによっては溶液
粘度が通常より大きく増大する現象が見出された。溶液
の粘度が増大すると、電極塗布工程での均一な膜厚が得
られ難くなるばかりか、活物質との混練時にゲル化して
しまい、製膜そのものが困難になる場合もあった。また
製膜が可能であったとしても、塗布乾燥後のバインダー
が非水系電解液中で膨潤度が大きくなる現象も見出され
た。バインダーの非水電解液中での膨潤が激しくなる
と、粉末電極材料(特に活物質)と金属電極箔や金属網
との接触抵抗や活物質間の接触抵抗が大きくなり、電池
の内部抵抗が増大する。また繰り返し充放電可能な二次
電池の場合には、内部抵抗の増大は充放電サイクル特性
の劣化につながり、ひいては電池寿命を短くする恐れが
ある。
When the above vinylidene fluoride polymer is used as a binder and dissolved in a polar organic solvent, the solution viscosity may increase more than usual depending on the lot of the solvent. Was found. When the viscosity of the solution increases, not only it becomes difficult to obtain a uniform film thickness in the electrode coating step, but also gelation occurs when kneading with the active material, which sometimes makes film formation itself difficult. Further, even if film formation is possible, a phenomenon has been found in which the binder after coating and drying has a large degree of swelling in the non-aqueous electrolyte solution. When the swelling of the binder in the non-aqueous electrolyte becomes severe, the contact resistance between the powder electrode material (especially active material) and the metal electrode foil or metal net or the contact resistance between the active materials increases, increasing the internal resistance of the battery. To do. Further, in the case of a secondary battery that can be repeatedly charged and discharged, an increase in internal resistance leads to deterioration of charge and discharge cycle characteristics, which may eventually shorten the battery life.

【0005】従って、本発明の主要な目的は、それ自体
粘度増加を起こすことなく安定であり、また非水系電解
液中で過度な膨潤を起すことなく安定な電池電極の形成
を可能とする、非水系電池電極形成用のフッ化ビニリデ
ン系重合体バインダー溶液、ならびにこれに粉末電極材
料を分散させた安定な特性の電極合剤を提供することに
ある。
Therefore, the main object of the present invention is to enable formation of a battery electrode which is stable without causing an increase in viscosity itself and is stable without causing excessive swelling in a non-aqueous electrolyte solution. It is intended to provide a vinylidene fluoride-based polymer binder solution for forming a non-aqueous battery electrode, and an electrode mixture having stable characteristics in which a powder electrode material is dispersed.

【0006】[0006]

【課題を解決するための手段】本発明の非水系電池電極
形成用のフッ化ビニリデン系重合体バインダー溶液は、
上記目的を達成するために開発されたものであり、フッ
化ビニリデン系重合体を有機溶媒に溶解してなり、その
一部を採取しイオン交換水で10倍に希釈して得た液の
pHが9以下になるように酸を添加して調製された非水
系電池電極形成用のフッ化ビニリデン系重合体バインダ
ー溶液を特徴とするものである。
The vinylidene fluoride-based polymer binder solution for forming a non-aqueous battery electrode of the present invention comprises:
It was developed in order to achieve the above-mentioned object, and it is a solution of a vinylidene fluoride polymer dissolved in an organic solvent, a part of which is collected and diluted 10 times with ion-exchanged water to obtain a pH of a liquid. And a vinylidene fluoride polymer binder solution for forming a non-aqueous battery electrode, which is prepared by adding an acid so that the ratio becomes 9 or less.

【0007】本発明の作用・効果について、若干付言す
る。本発明者等が鋭意研究した結果、上述したフッ化ビ
ニリデン系重合体バインダー溶液における異常な粘度上
昇の原因は、系の酸−アルカリ度と関係することが見出
された。すなわち、上記したフッ化ビニリデン系重合体
の有機溶媒溶液の酸−アルカリ度を直接に判定すること
は困難であるが、その一部を採取しイオン交換水で10
倍に希釈して得た液のpHが一つの目安となる。そし
て、粘度上昇の生じた系においては、このようにして測
定した液のpHが9を超えていることが判明した。そし
て、これはそれ自体は既知の現象であるフッ化ビニリデ
ン系重合体のアルカリ性の媒体中における脱フッ酸反応
に関連しており、バインダー性能にも直接関係している
こと、また、フッ化ビニリデン系重合体に対し良好な溶
解性を示す極性溶媒の多くは、N−メチルピロリドン、
ジメチルフォルムアミド等の含窒素有機溶媒であり、溶
媒のロット毎による増粘現象の有無、程度の差は、この
ような含窒素有機溶媒の製造時あるいはその後の保管中
におけるアミン等のアルカリ性物質の残留、生成、もし
くは遊離による溶媒のアルカリ度の上昇と関連している
と解される。なおフッ化ビニリデン系重合体からの脱フ
ッ酸によりバインダーとしての耐溶剤性(耐膨潤性)が
低下するのは、脱フッ素部位に酸素が付加しやすく、結
果的に非水系電解液への親和性が増大するため、あるい
は異種結合の増大が良好な耐溶剤性を与える有力なファ
クターとしての重合体の結晶性を低下させたためと解さ
れる。本発明は、このような解析に基づき、上述したフ
ッ化ビニリデン系重合体バインダー溶液の増粘現象を伴
う不都合が、酸を添加して系のpHを9以下に低下させ
ることにより有効に抑制されることの知見に基づく。
The operation and effect of the present invention will be slightly added. As a result of intensive studies by the present inventors, it was found that the cause of the above-mentioned abnormal increase in viscosity of the vinylidene fluoride-based polymer binder solution is related to the acid-alkalinity of the system. That is, it is difficult to directly determine the acid-alkalinity of the above-mentioned vinylidene fluoride-based polymer solution in an organic solvent, but a part of the acid-alkalinity is sampled and deionized with 10
The pH of the solution obtained by doubling the dilution is one measure. It was found that the pH of the liquid thus measured exceeded 9 in the system in which the viscosity increased. This is related to the dehydrofluoric acid reaction of vinylidene fluoride-based polymer in an alkaline medium, which is a known phenomenon per se, and is also directly related to the binder performance. Most of polar solvents having good solubility in the base polymer are N-methylpyrrolidone,
It is a nitrogen-containing organic solvent such as dimethylformamide, and the presence or absence of the thickening phenomenon depending on the lot of the solvent and the degree of the difference are different from those of alkaline substances such as amines during the production or subsequent storage of the nitrogen-containing organic solvent. It is understood to be associated with an increase in the alkalinity of the solvent due to residual, formation or liberation. Note that the solvent resistance (swelling resistance) of the binder decreases due to dehydrofluoric acid from the vinylidene fluoride-based polymer because oxygen is easily added to the defluorination site, and as a result, the affinity for the non-aqueous electrolyte solution is increased. It is considered that the crystallinity of the polymer is lowered due to an increase in the polymer property or an increase in the number of different kinds of bonds as a powerful factor for providing good solvent resistance. Based on such analysis, the present invention effectively suppresses the above-mentioned inconvenience associated with the thickening phenomenon of the vinylidene fluoride polymer binder solution by adding an acid to lower the pH of the system to 9 or less. Based on the knowledge of things.

【0008】[0008]

【発明の実施の形態】本発明において用いられるフッ化
ビニリデン系重合体には、フッ化ビニリデンの単独重合
体、共重合体およびこれらの変性物が含まれる。フッ化
ビニリデンの単独重合体は、非水系電解液に対する耐久
性、特に耐膨潤性、の観点では好ましい。しかし、金属
等の電極基体との接着性が若干不足気味であるため、よ
り好ましくは、他のモノマーとの共重合体、特に不飽和
二塩基酸のモノエステル、ビニレンカーボネートあるい
はエポキシ含有ビニル単量体等との共重合によりカルボ
キシル基、カーボネート基、エポキシ基等の極性基を導
入した共重合体(特開平6−172452号公報等)が
好ましく用いられる。またこれらフッ化ビニリデンの単
独または共重合体を溶解または膨潤する溶媒中で、アミ
ノ基またはメルカプト基等のフッ化ビニリデン系重合体
と反応性基と加水分解性基を併有するシラン系カップリ
ング剤あるいはチタネート系カップリング剤中で処理し
てなる変性フッ化ビニリデン系重合体(特開平6−93
025号)も好ましく用いられる。但し、全体として非
水系電解液に対する耐膨潤性を良好に維持するために、
非処理のフッ化ビニリデン単位を90モル%以上、特に
95モル%以上の範囲で維持することが好ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The vinylidene fluoride polymer used in the present invention includes vinylidene fluoride homopolymers, copolymers and modified products thereof. A vinylidene fluoride homopolymer is preferable from the viewpoint of durability against a non-aqueous electrolyte, particularly swelling resistance. However, since the adhesion to an electrode substrate such as a metal is slightly insufficient, it is more preferable to use a copolymer with another monomer, particularly a monoester of an unsaturated dibasic acid, vinylene carbonate or an epoxy-containing vinyl monomer. A copolymer in which a polar group such as a carboxyl group, a carbonate group or an epoxy group is introduced by copolymerization with a polymer or the like (JP-A-6-172452, etc.) is preferably used. Also, in a solvent that dissolves or swells a vinylidene fluoride homopolymer or a copolymer, a silane coupling agent having both a vinylidene fluoride polymer such as an amino group or a mercapto group, a reactive group and a hydrolyzable group. Alternatively, a modified vinylidene fluoride-based polymer obtained by treatment in a titanate-based coupling agent (JP-A-6-93).
No. 025) is also preferably used. However, in order to maintain good swelling resistance to the non-aqueous electrolyte as a whole,
It is preferable to maintain the untreated vinylidene fluoride unit in the range of 90 mol% or more, particularly 95 mol% or more.

【0009】フッ化ビニリデン系重合体は、固有粘度
(樹脂4gを1リットルのN,N−ジメチルホルムアミ
ドに溶解させた溶液の30℃における対数粘度)が、
0.5以上、更には0.5〜2.0、特に0.8〜1.
5、の範囲内の値を有することが好ましい。
The vinylidene fluoride polymer has an intrinsic viscosity (logarithmic viscosity at 30 ° C. of a solution of 4 g of resin dissolved in 1 liter of N, N-dimethylformamide)
0.5 or more, more preferably 0.5 to 2.0, especially 0.8 to 1.
It is preferable to have a value within the range of 5.

【0010】上記フッ化ビニリデン系重合体を溶解し
て、本発明のバインダー溶液を得るために用いられる有
機溶媒は、好ましくは極性のものであり、例えばN−メ
チル−2−ピロリドン、ジメチルフォルムアミド、N,
N−ジメチルアセトアミド、N,N−ジメチルスルフォ
キシド、ヘキサメチルフォスフォアミド、ジオキサン、
テトラヒドロフラン、テトラメチルウレア、トリエチル
フォスフェイト、トリメチルフォスフェイト、などが挙
げられる。これら有機溶媒は単独でまたは二種以上混合
して用いられる。前述したように、フッ化ビニリデン系
重合体の良溶媒の多くは含窒素溶媒であり、またバイン
ダー溶液の粘度上昇の原因となるアルカリ性物質を生成
し易いものも含窒素有機溶媒である。従って、本発明で
好ましく用いられる有機溶媒は含窒素有機溶媒である
が、非窒素系の有機溶媒についても本発明に従い、酸を
添加してpHを調製しておくことは、何らかの理由によ
るその後のpH増加に伴う不都合を回避できるので好ま
しい。このような非窒素系の良溶媒としては、前述した
ジオキサン、テトラヒドロフラン、トリアルキルホスフ
ェート等があり、単独で又は含窒素有機溶媒と混合して
好適に使用される。
The organic solvent used to obtain the binder solution of the present invention by dissolving the above vinylidene fluoride polymer is preferably a polar solvent such as N-methyl-2-pyrrolidone or dimethylformamide. , N,
N-dimethylacetamide, N, N-dimethylsulfoxide, hexamethylphosphamide, dioxane,
Examples include tetrahydrofuran, tetramethylurea, triethyl phosphate, trimethyl phosphate, and the like. These organic solvents may be used alone or in admixture of two or more. As described above, most of good solvents for vinylidene fluoride-based polymers are nitrogen-containing solvents, and those that easily generate an alkaline substance that causes an increase in viscosity of the binder solution are also nitrogen-containing organic solvents. Therefore, the organic solvent preferably used in the present invention is a nitrogen-containing organic solvent, but for a non-nitrogen-based organic solvent, it is necessary to add an acid to adjust the pH according to the present invention. This is preferable because it is possible to avoid the inconvenience associated with the increase in pH. Examples of such a non-nitrogen-based good solvent include the above-mentioned dioxane, tetrahydrofuran, trialkyl phosphate and the like, which are preferably used alone or mixed with a nitrogen-containing organic solvent.

【0011】本発明のバインダー溶液を得るに当り、こ
れら有機溶媒100重量部当り、前記フッ化ビニリデン
系重合体を0.1〜20重量部、特に1〜15重量部、
の割合で溶解することが好ましい。0.1重量部未満で
は、溶液中での重合体の占める割合が小さすぎ、バイン
ダーとしての効果が得られない。また、20重量部を越
えると、溶液の粘度が高くなり過ぎて電極合剤の調整が
困難になる。
To obtain the binder solution of the present invention, 0.1 to 20 parts by weight, especially 1 to 15 parts by weight of the above vinylidene fluoride polymer is added to 100 parts by weight of these organic solvents.
It is preferable to dissolve in the ratio of If it is less than 0.1 part by weight, the proportion of the polymer in the solution is too small, and the effect as a binder cannot be obtained. On the other hand, if it exceeds 20 parts by weight, the viscosity of the solution becomes too high and it becomes difficult to adjust the electrode mixture.

【0012】本発明に従い、酸を添加後のバインダー溶
液について、その溶液の一部を採取してイオン交換水に
よる10倍希釈液のpHが9以下になるように調整す
る。
According to the present invention, with respect to the binder solution after addition of the acid, a part of the solution is sampled and adjusted so that the pH of the 10-fold diluted solution with ion-exchanged water is 9 or less.

【0013】添加される酸としては、基本的には限定さ
れないが、電極合剤として塗布し、乾燥する工程中に分
解や蒸発により飛散して成型電極中に残留しないものが
好ましく、また電極活物質と反応し難いものが好まし
い。この点で、塩酸や硫酸などの無機酸は電極活物質と
反応し易く必ずしも好ましくない。特に黒鉛などの無機
物と層間化合物を形成し易い電極活物質を用いる場合に
は、層間化合物を形成し難い大きな分子直径を有する有
機酸を用いることが好ましい。乾燥工程での温度領域
(通常PVDFの融点である175℃以下)で高い蒸気
圧を有するか、または分解飛散するものが好ましい。こ
のような観点で好ましく用いられる有機酸の例として
は、アクリル酸、ギ酸、クエン酸、酢酸、シュウ酸、乳
酸、ピルピン酸、マロン酸、プロピオン酸、マレイン
酸、酪酸等が挙げられる。
The acid to be added is not particularly limited, but it is preferable that the acid is scattered as a result of decomposition or evaporation during the step of applying as an electrode mixture and drying, and does not remain in the molded electrode. Those that are difficult to react with the substance are preferable. In this respect, inorganic acids such as hydrochloric acid and sulfuric acid are not always preferable because they easily react with the electrode active material. Particularly when an electrode active material that easily forms an intercalation compound with an inorganic substance such as graphite is used, it is preferable to use an organic acid having a large molecular diameter that makes it difficult to form an intercalation compound. It is preferable that it has a high vapor pressure or decomposes and scatters in the temperature range of the drying step (usually 175 ° C. or lower which is the melting point of PVDF). Examples of organic acids that are preferably used from this viewpoint include acrylic acid, formic acid, citric acid, acetic acid, oxalic acid, lactic acid, pyrupic acid, malonic acid, propionic acid, maleic acid, butyric acid and the like.

【0014】フッ化ビニリデン系重合体溶液中に酸を添
加する方法としては、予め有機溶媒に酸を添加して溶媒
のpHを調整してから重合体を溶解する方法が好ましい
が、有機溶媒に重合体を溶解する際に酸を同時に添加し
て溶解する方法や、重合体を溶解し終わってから溶液中
に酸を添加する方法であっても良い。
As a method of adding an acid to the vinylidene fluoride polymer solution, a method of previously adding an acid to an organic solvent to adjust the pH of the solvent and then dissolving the polymer is preferable. A method of adding an acid at the same time to dissolve the polymer to dissolve it, or a method of adding the acid to the solution after the polymer is completely dissolved may be used.

【0015】酸の添加量は、添加後のバインダー溶液の
イオン交換水による10倍希釈液のpH(好ましい態様
に従い予め有機溶媒に酸添加したときの希釈液pHとほ
ぼ一致)が、9以下、好ましくは7.5以下、とする量
が添加される。下限は特に限定されないが、一般に3程
度までで、それ以上添加しても特に効果の増大は期待で
きない。但し、上述した好ましい態様である有機酸の場
合には、電極の塗布、乾燥による成形工程で分解揮散す
るので、過剰に加えても有害ではない。予め、酸を添加
する前の有機溶媒あるいはバインダー溶液のpHが9以
下となっている場合でも、その後の溶媒の分解等の何ら
かの理由によるpH上昇に対する緩衝効果を期待して、
一定量の酸を添加することが好ましい。この場合の酸の
添加量は、バインダー溶液1リットル中に、100pp
m以上、特に300〜10,000ppm添加しておく
ことが好ましい。このような態様のときには、残留して
も害の殆どない有機酸を添加することが特に好ましい。
The amount of acid added is such that the pH of a 10-fold diluted solution of the binder solution after addition with ion-exchanged water (substantially equal to the diluted solution pH when an acid is previously added to an organic solvent according to a preferred embodiment) is 9 or less, It is preferably added in an amount of 7.5 or less. The lower limit is not particularly limited, but is generally up to about 3, and addition of more than this cannot be expected to increase the effect. However, in the case of the organic acid, which is the preferred embodiment described above, since it decomposes and volatilizes in the molding process by coating and drying the electrode, it is not harmful even if added in excess. Even if the pH of the organic solvent or binder solution before adding the acid is 9 or less in advance, expect a buffering effect against the pH increase due to some reason such as the subsequent decomposition of the solvent,
It is preferred to add a fixed amount of acid. In this case, the addition amount of acid is 100 pp in 1 liter of binder solution.
It is preferable to add at least m, especially 300 to 10,000 ppm. In such a mode, it is particularly preferable to add an organic acid which causes little harm even if it remains.

【0016】上記のようにして得られた本発明のフッ化
ビニリデン系重合体バインダー溶液に、粉末電極材料
(活物質および必要に応じて加えられる導電材、その他
の助剤)を分散混合することにより電極合剤が得られ
る。
The powdery electrode material (active material and conductive material added as necessary, other auxiliaries) is dispersed and mixed in the vinylidene fluoride polymer binder solution of the present invention obtained as described above. By this, an electrode mixture is obtained.

【0017】活物質としては、正極の場合は、一般式L
iMY2 (Mは、Co、Ni、Fe、Mn、Cr、V等
の遷移金属の少なくとも一種:YはO、S等のカルコゲ
ン元素)で表わされる複合金属カルコゲン化合物、特に
LiCoO2 をはじめとする複合金属酸化物やLiMn
2 4 などのスピネル構造をとる複合金属酸化物が好ま
しい。負極の場合は、黒鉛、活性炭、あるいはフェノー
ル樹脂やピッチ等を焼成炭化したもの等の炭素質物質が
活物質としては好ましい。
As the active material, in the case of the positive electrode, the general formula L is used.
A complex metal chalcogen compound represented by iMY 2 (M is at least one kind of transition metal such as Co, Ni, Fe, Mn, Cr and V: Y is a chalcogen element such as O and S), particularly LiCoO 2. Complex metal oxides and LiMn
A composite metal oxide having a spinel structure such as 2 O 4 is preferable. In the case of the negative electrode, graphite, activated carbon, or a carbonaceous material such as one obtained by firing and carbonizing phenol resin or pitch is preferable as the active material.

【0018】導電材はLiCoO2 等の電子伝導性の小
さい活物質を使用する場合に電極合剤層の導電性を向上
する目的で添加するもので、カーボンブラック、黒鉛微
粉末あるいは繊維等の炭素質物質やニッケル、アルミニ
ウム等の金属微粉末あるいは、繊維が使用される。活物
質として導電性の大きい炭素質物質を用いる場合はこれ
らの導電材は使用する必要がない。
The conductive material is added for the purpose of improving the conductivity of the electrode mixture layer when an active material having a low electron conductivity such as LiCoO 2 is used, and carbon such as carbon black, graphite fine powder or fibers is used. Fine materials, fine metal powders such as nickel and aluminum, or fibers are used. When a carbonaceous material having high conductivity is used as the active material, it is not necessary to use these conductive materials.

【0019】本発明の電極合剤においては、フッ化ビニ
リデン系重合体100重量部に対し、0.1〜50重量
部、特に1〜20重量部の粉末電極材料を混合すること
が好ましい。
In the electrode mixture of the present invention, it is preferable to mix 0.1 to 50 parts by weight, especially 1 to 20 parts by weight of the powder electrode material with 100 parts by weight of the vinylidene fluoride polymer.

【0020】形成された電極合剤を、鉄、ステンレス
鋼、鋼、銅、アルミニウム、ニッケル、チタン等の金属
箔あるいは金属網等からなり、厚さが5〜100μm、
小規模の場合には例えば5〜20μmとなるような集電
体の少なくとも一面、好ましくは両面に塗布し、例えば
50〜170℃で乾燥して、例えば小規模の場合厚さが
10〜1000μmの電極合剤層を形成することによ
り、電極が形成される。
The formed electrode mixture is made of a metal foil such as iron, stainless steel, steel, copper, aluminum, nickel, titanium, or a metal net, and has a thickness of 5 to 100 μm.
In the case of a small scale, it is applied on at least one side, preferably both sides, of a current collector having a thickness of, for example, 5 to 20 μm, and dried, for example, at 50 to 170 ° C. The electrode is formed by forming the electrode mixture layer.

【0021】本発明のバインダー溶液および電極合剤を
用いて形成される電極は、非水系電池、特にリチウムイ
オン電池の電極として用いることが好ましく、この際用
いられる電解液としては、例えばリチウム塩などの電解
質を非水系溶媒(有機溶媒)に溶解したものを用いるこ
とができる。
The electrode formed by using the binder solution and the electrode mixture of the present invention is preferably used as an electrode of a non-aqueous battery, especially a lithium ion battery, and an electrolyte used in this case is, for example, a lithium salt. It is possible to use a solution obtained by dissolving the above electrolyte in a non-aqueous solvent (organic solvent).

【0022】ここで電解質としては、LiPF6 、Li
AsF6 、LiClO3 、LiBF4 、CH3 SO3
i、CF3 SO3 Li、LiCl、LiBr等がある。
また、電解質の有機溶媒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、1,2−ジメトキシエタ
ン、1,2−ジエトキシエタン、ジメチルカーボネー
ト、ジエチルカーボネート、メチルエチルカーボネー
ト、γ−プチルラクトン、プロピオン酸メチル、プロピ
オン酸エチル、およびこれらの混合溶媒などが用いられ
るが、必ずしもこれらに限定されるものではない。
Here, as the electrolyte, LiPF 6 , Li
AsF 6 , LiClO 3 , LiBF 4 , CH 3 SO 3 L
i, CF 3 SO 3 Li, LiCl, LiBr and the like.
Further, as the organic solvent of the electrolyte, propylene carbonate, ethylene carbonate, 1,2-dimethoxyethane, 1,2-diethoxyethane, dimethyl carbonate, diethyl carbonate, methyl ethyl carbonate, γ-putyl lactone, methyl propionate, propionic acid. Ethyl, a mixed solvent thereof, and the like are used, but not limited thereto.

【0023】[0023]

【実施例】以下、実施例、比較例により本発明を更に具
体的に説明する。
The present invention will be described more specifically with reference to examples and comparative examples.

【0024】(フッ化ビニリデン系重合体の調製)特開
平6−172452号公報に記載の実施例1に従い、以
下のようにしてカルボキシル基含有フッ化ビニリデン系
重合体を得た。
(Preparation of Vinylidene Fluoride Polymer) According to Example 1 described in JP-A-6-172452, a vinylidene fluoride polymer containing a carboxyl group was obtained as follows.

【0025】内容量2リットルのオートクレーブに、イ
オン交換水1040g、メチルセルロース0.8g、酢
酸エチル2.5g、ジイソプロピルパーオキシジカーボ
ネート4g、フッ化ビニリデン396g、マレイン酸モ
ノメチルエステル4gを仕込み(フッ化ビニリデン:マ
レイン酸モノメチルエステル=100:1.01)、2
8℃で47時間懸濁重合を行った。重合完了後、重合体
スラリーを脱水、水洗後80℃で20時間乾燥して重合
体粉末を得た。
In an autoclave having a content of 2 liters, 1040 g of ion-exchanged water, 0.8 g of methyl cellulose, 2.5 g of ethyl acetate, 4 g of diisopropyl peroxydicarbonate, 396 g of vinylidene fluoride and 4 g of maleic acid monomethyl ester were charged (vinylidene fluoride). : Maleic acid monomethyl ester = 100: 1.01), 2
Suspension polymerization was carried out at 8 ° C. for 47 hours. After completion of the polymerization, the polymer slurry was dehydrated, washed with water and dried at 80 ° C. for 20 hours to obtain a polymer powder.

【0026】重合率は90重量%で、得られた重合体
は、固有粘度1.1、カルボニル基含有量1.2×10
-4モル/gであった。
The polymerization rate was 90% by weight, and the obtained polymer had an intrinsic viscosity of 1.1 and a carbonyl group content of 1.2 × 10.
-4 mol / g.

【0027】(有機溶媒)市販のN−メチル−2−ピロ
リドンの20ロットにわたるものを、約3カ月間室温で
保存したものを用いた。以下、「NMP」と略記する。
イオン交換水による10倍希釈液のpHは、6.5〜1
1.0の範囲にわたっていた。
(Organic solvent) A commercially available product of 20 lots of N-methyl-2-pyrrolidone stored for about 3 months at room temperature was used. Hereinafter, it is abbreviated as “NMP”.
The pH of the 10-fold diluted solution with ion-exchanged water is 6.5 to 1
It was in the range of 1.0.

【0028】比較例1 イオン交換水による10倍希釈液のpHが9.5を示し
たロットのNMPに、上記フッ化ビニリデン系重合体を
13重量%の濃度となるように温度50℃で溶解して、
バインダー溶液を得た。
Comparative Example 1 The vinylidene fluoride polymer was dissolved in NMP of a lot in which the pH of a 10-fold diluted solution with ion-exchanged water showed 9.5 at a temperature of 50 ° C. so that the concentration of the vinylidene fluoride polymer was 13% by weight. do it,
A binder solution was obtained.

【0029】実施例1 上記比較例1で用いたロットのNMPにマレイン酸を1
000ppm添加し、再度イオン交換水による10倍希
釈液のpHを測定すると3.2であった。次にこのマレ
イン酸を添加したNMPに、上記フッ化ビニリデン系重
合体を比較例1と同じく13重量%の濃度となるように
溶解して、バインダー溶液を得た。
Example 1 Maleic acid was added to the lot of NMP used in Comparative Example 1 above.
000 ppm was added, and the pH of the 10-fold diluted solution with ion-exchanged water was measured again, and it was 3.2. Next, the vinylidene fluoride polymer was dissolved in NMP containing maleic acid so as to have a concentration of 13% by weight as in Comparative Example 1 to obtain a binder solution.

【0030】(粘度およびフッ素イオン濃度測定)上記
比較例1および実施例1で得られたバインダー溶液の粘
度を、それぞれJIS K7117に準拠した回転粘度
計を用いて測定した。またフッ素イオン(F- )の濃度
も測定した。
(Measurement of Viscosity and Fluorine Ion Concentration) The viscosities of the binder solutions obtained in Comparative Example 1 and Example 1 were measured using a rotary viscometer in accordance with JIS K7117. The concentration of fluorine ion (F ) was also measured.

【0031】(フィルム形成および膨潤テスト)上記比
較例1および実施例1のバインダー溶液を、それぞれガ
ラス板上にキャストし、130℃で2時間乾燥し、厚さ
約200μmのフィルムを得た。
(Film Formation and Swelling Test) The binder solutions of Comparative Example 1 and Example 1 were cast on glass plates and dried at 130 ° C. for 2 hours to obtain a film having a thickness of about 200 μm.

【0032】次いでこれらフィルムを、LiClO
4 8.8重量部を、プロピレンカーボネート53.6重
量部とジメトキシエタン37.6重量部の混合液に溶解
して得た電解液に、それぞれ浸漬し、70℃、72時間
の浸漬を行い、途中24時間毎にキャストフィルムの重
量増加率(増加重量/原フィルム重量×100)による
膨潤度を求めた。
Next, these films were treated with LiClO.
4 8.8 parts by weight was immersed in an electrolytic solution obtained by dissolving 53.6 parts by weight of propylene carbonate and 37.6 parts by weight of dimethoxyethane, respectively, and immersed at 70 ° C. for 72 hours, The swelling degree was calculated every 24 hours on the way by the weight increase rate of the cast film (increase weight / raw film weight × 100).

【0033】上記測定結果をまとめて、下表1に示す。The above measurement results are summarized in Table 1 below.

【0034】[0034]

【表1】 [Table 1]

【0035】上表1の結果は、NMPをそのまま用いた
比較例のフッ化ビニリデン系重合体バインダー溶液に比
べて、1000ppmのマレイン酸を添加して得られた
フッ化ビニリデン系重合体バインダー溶液は、粘度上
昇、フッ素イオン濃度がともに低く、安定であること、
また非水電池用電解液に対する耐膨潤性が顕著に改善さ
れていることがわかる。
The results in Table 1 above show that the vinylidene fluoride-based polymer binder solution obtained by adding 1000 ppm of maleic acid was compared to the vinylidene fluoride-based polymer binder solution of the comparative example in which NMP was used as it was. , Viscosity increase, low fluoride ion concentration, and stable,
It is also found that the swelling resistance to the electrolyte for non-aqueous batteries is remarkably improved.

【0036】比較例2 イオン交換水による10倍希釈液のpHが10.9を示
したロットのNMPに上記カルボキシル基含有フッ化ビ
ニリデン系重合体を13重量%の濃度となるように溶解
してバインダー溶液を形成した。
Comparative Example 2 The above vinylidene fluoride polymer containing a carboxyl group was dissolved in NMP of a lot in which the pH of a 10-fold diluted solution with ion-exchanged water showed 10.9 to a concentration of 13% by weight. A binder solution was formed.

【0037】実施例2 上記比較例2と同じロットのNMPに、1000ppm
のマロン酸を添加し、その後上記カルボキシル基含有フ
ッ化ビニリデン系重合体を13重量%の濃度となるよう
に溶解して、バインダー溶液を形成した。
Example 2 NMP of the same lot as in Comparative Example 2 was added with 1000 ppm.
Malonic acid was added, and then the above vinylidene fluoride polymer containing a carboxyl group was dissolved to a concentration of 13% by weight to form a binder solution.

【0038】上記比較例2および実施例2のバインダー
溶液から、それぞれ上記実施例1と同様にフィルムを形
成し、同様に70℃、72時間の電解液中浸漬膨潤テス
トを行った。72時間後の膨潤度は以下の通りであっ
た。
A film was formed from each of the binder solutions of Comparative Example 2 and Example 2 in the same manner as in Example 1 above, and the immersion swelling test in the electrolytic solution was conducted at 70 ° C. for 72 hours. The degree of swelling after 72 hours was as follows.

【0039】[0039]

【表2】 [Table 2]

【0040】比較例3 イオン交換水による10倍希釈液のpHが、9.5を示
したロットのNMPにフッ化ビニリデンホモポリマー
(「KF1100」、呉羽化学工業(株)製)を13重
量%の濃度となるように温度50℃で溶解して、バイン
ダー溶液を得た。
Comparative Example 3 13% by weight of vinylidene fluoride homopolymer (“KF1100”, manufactured by Kureha Chemical Industry Co., Ltd.) was added to NMP in a lot in which the pH of a 10-fold diluted solution with ion-exchanged water was 9.5. Was dissolved at a temperature of 50 ° C. to obtain a binder solution.

【0041】実施例3 上記比較例3で用いたロットのNMPにマレイン酸を1
000ppm添加し、再度イオン交換水による10倍希
釈液のpHを測定すると3.2であった。次にこのマレ
イン酸を添加したNMPに、上記比較例1で用いたフッ
化ビニリデンホモポリマーを同じく13重量%の濃度と
なるように溶解してバインダー溶液を得た。
Example 3 Maleic acid was added to 1 lot of NMP used in Comparative Example 3 above.
000 ppm was added, and the pH of the 10-fold diluted solution with ion-exchanged water was measured again, and it was 3.2. Next, the vinylidene fluoride homopolymer used in Comparative Example 1 was dissolved in the NMP containing maleic acid so as to have a concentration of 13% by weight to obtain a binder solution.

【0042】上記比較例3、実施例3で得られたバイン
ダー溶液について実施例1と同様に粘度およびフィルム
膨潤度を測定した結果を下表3に示す。
The results of measuring the viscosity and the film swelling degree of the binder solutions obtained in Comparative Example 3 and Example 3 as in Example 1 are shown in Table 3 below.

【0043】[0043]

【表3】 [Table 3]

【0044】ここでも酸添加による、良好なバインダー
溶液の粘度上昇防止効果、フィルム耐膨潤性の向上効果
が認められる。
Also in this case, the effect of preventing the viscosity increase of the binder solution and the effect of improving the swelling resistance of the film are confirmed by the addition of the acid.

【0045】実施例4、比較例4 上記実施例1、比較例1で得られたフィルムを、それぞ
れ、LiPF6 11.6重量%、エチレンカーボネート
51.0重量%およびジエチルカーボネート37.4重
量%からなる電解液に、70℃で72時間浸漬し、放置
した。浸漬後のフィルムの膨潤度(膨潤による重量増加
率)は、それぞれ18重量%および24重量%であっ
た。
Example 4, Comparative Example 4 The films obtained in Example 1 and Comparative Example 1 were respectively coated with 11.6% by weight of LiPF 6 , 51.0% by weight of ethylene carbonate and 37.4% by weight of diethyl carbonate. It was dipped in an electrolytic solution consisting of at 70 ° C. for 72 hours and left to stand. The degree of swelling of the film after immersion (the rate of increase in weight due to swelling) was 18% by weight and 24% by weight, respectively.

【0046】[0046]

【発明の効果】上述したように、本発明によれば、フッ
化ビニリデン系重合体を有機溶媒に溶解して非水系電池
電極形成用のバインダー溶液を形成するに際し、酸、好
ましくは有機酸を添加することにより、従来はしばしば
問題となったバインダー溶液の粘度上昇、ならびに形成
される電極中でのバインダーの電解液による膨潤のため
のバインダ効果の低減を効果的に防止することが可能と
なる。
As described above, according to the present invention, when a vinylidene fluoride polymer is dissolved in an organic solvent to form a binder solution for forming a non-aqueous battery electrode, an acid, preferably an organic acid, is added. By adding it, it becomes possible to effectively prevent the increase in the viscosity of the binder solution, which has often been a problem in the past, and the reduction in the binder effect due to the swelling of the binder in the formed electrode by the electrolytic solution. .

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 フッ化ビニリデン系重合体を有機溶媒に
溶解してなり、その一部を採取しイオン交換水で10倍
に希釈して得た液のpHが9以下になるように酸を添加
して調製された非水系電池電極形成用のフッ化ビニリデ
ン系重合体バインダー溶液。
1. A solution of a vinylidene fluoride polymer dissolved in an organic solvent, a portion of which is sampled and diluted 10 times with ion-exchanged water to obtain an acid so that the pH of the resulting solution is 9 or less. A vinylidene fluoride polymer binder solution for forming a non-aqueous battery electrode, which is prepared by adding it.
【請求項2】 フッ化ビニリデン系重合体が、95モル
%以上のフッ化ビニリデンと他のモノマーとの共重合体
またはフッ化ビニリデンの単独または共重合体の変性物
である請求項1に記載のバインダー溶液。
2. The vinylidene fluoride-based polymer is a copolymer of 95 mol% or more of vinylidene fluoride and another monomer, or a vinylidene fluoride homopolymer or a modified product of the copolymer. Binder solution.
【請求項3】 フッ化ビニリデン系重合体が、カルボキ
シル基含有フッ化ビニリデン系重合体である請求項1に
記載のバインダー溶液。
3. The binder solution according to claim 1, wherein the vinylidene fluoride-based polymer is a carboxyl group-containing vinylidene fluoride-based polymer.
【請求項4】 前記酸が有機酸である請求項1〜3のい
ずれかに記載のバインダー溶液。
4. The binder solution according to claim 1, wherein the acid is an organic acid.
【請求項5】 前記有機溶媒が含窒素有機溶媒である請
求項1〜4のいずれかに記載のバインダー溶液。
5. The binder solution according to claim 1, wherein the organic solvent is a nitrogen-containing organic solvent.
【請求項6】 請求項1〜5のいずれかに記載のバイン
ダー溶液中に粉末電極材料を分散させてなる電極合剤。
6. An electrode mixture obtained by dispersing a powder electrode material in the binder solution according to claim 1.
JP35078295A 1995-12-26 1995-12-26 Battery binder solution and electrode mixture Expired - Lifetime JP3540080B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP35078295A JP3540080B2 (en) 1995-12-26 1995-12-26 Battery binder solution and electrode mixture
US08/779,955 US6200703B1 (en) 1995-12-26 1996-12-23 Binder solution and electrode-forming composition for non-aqueous-type battery
EP96309481A EP0782208B1 (en) 1995-12-26 1996-12-24 Binder solution and electrode-forming composition for non-aqueous-type battery
CA002193935A CA2193935C (en) 1995-12-26 1996-12-24 Binder solution and electrode-forming composition for non-aqueous-type battery
DE69635888T DE69635888T8 (en) 1995-12-26 1996-12-24 Binder solution and electrode forming composition for non-aqueous battery
KR1019960072262A KR100263735B1 (en) 1995-12-26 1996-12-26 Binder solution and electrode-forming composition for non-aqueous-type battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35078295A JP3540080B2 (en) 1995-12-26 1995-12-26 Battery binder solution and electrode mixture

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