Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6019624B2 - Battery separator and its manufacturing method - Google Patents
[go: Go Back, main page]

JPS6019624B2 - Battery separator and its manufacturing method - Google Patents

Battery separator and its manufacturing method

Info

Publication number
JPS6019624B2
JPS6019624B2 JP54030691A JP3069179A JPS6019624B2 JP S6019624 B2 JPS6019624 B2 JP S6019624B2 JP 54030691 A JP54030691 A JP 54030691A JP 3069179 A JP3069179 A JP 3069179A JP S6019624 B2 JPS6019624 B2 JP S6019624B2
Authority
JP
Japan
Prior art keywords
graft
grafting
film
monomer
grafting rate
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.)
Expired
Application number
JP54030691A
Other languages
Japanese (ja)
Other versions
JPS55122361A (en
Inventor
末男 町
功 石垣
高信 須郷
紀夫 岡田
和雄 村田
紫朗 丹宗
敬次 妹尾
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.)
Yuasa Corp
Original Assignee
Yuasa 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 Yuasa Corp filed Critical Yuasa Corp
Priority to JP54030691A priority Critical patent/JPS6019624B2/en
Publication of JPS55122361A publication Critical patent/JPS55122361A/en
Publication of JPS6019624B2 publication Critical patent/JPS6019624B2/en
Expired legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403Manufacturing processes of separators, membranes or diaphragms
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417Polyolefins
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/497Ionic conductivity
    • 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

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Cell Separators (AREA)

Description

【発明の詳細な説明】 本発明は電池用セパレータおよびその製造法に係るもの
で、寸法安定性の優れたセパレータを提供するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a battery separator and a method for manufacturing the same, and provides a separator with excellent dimensional stability.

近年、電池の高性能化および長寿命化の要求にともない
、耐久性の優れたセパレー夕、特にポリエチレンフィル
ムを基材とし、これをイオン交換基を有する単量体をグ
ラフト重合したグラフト膜が、電池のセパレータとして
検討されている。
In recent years, with the demand for higher performance and longer life of batteries, highly durable separators, especially graft membranes made of polyethylene film as a base material and graft polymerized with monomers having ion exchange groups, have been developed. It is being considered as a battery separator.

これらのグラフト膜はポリエチレン主鎖にイオン交換基
を有する単量体が枝ポリマーを形成することにより、膜
中に電解液を吸収し、イオン伝導性が得られる。イオン
伝導性は単量体のグラフト率が高くなるとともに高くな
る。一方電解液を膿中に包含するために、膜は膨潤し、
月莫の縦、横、厚み、方向にその寸法が変化する。この
膨滴による寸法変化は、グラフト率の増加とともに大き
くなる。通常の電池のセパレータとして使用し得るイオ
ン伝導性(電気抵抗)を有する膜の電解液中での寸法変
化は15〜20%著しくは、25%にも達する。この様
な著しい寸法変化、特に縦および横方向の寸法変化は限
られた寸法および容積の小型電池においては、電池組立
作業が極めて困難となる。また比較的寸法変化が許容さ
れる大型電池においても、電解液注液後に極間に挟持さ
れたセパレータが膨潤し、極間で不均一な空隙を生じガ
ス留りが生じる原因となり、電池性能を低下させるなど
の欠点があった。従来これらのグラフト膜は、かかる欠
点を除去すべ〈あらかじめ機械的に腰を伸張させた状態
で、電池電解液に寸法安定性(特に縦、横方向に)を有
する他のセパレータ、例えばセロハン、合成樹脂からな
る徴孔性フィルムなどと貼り合わせることにより、電解
液による膨潤変化を防止していた。このために、グラフ
ト膜は、単独で使用されることはなく他のセパレータと
の併用がなされていた。したがってグラフト膜の優れた
性能にもかかわらず、電池の高性能化、特に容積効率の
向上にグラフト膜は有効に効果を発揮していなかった。
本発明は、従来の上記欠点を除去するもので、特に寸法
安定性の優れたセパレータを提供するものである。
In these graft membranes, monomers having ion exchange groups in the polyethylene main chain form branch polymers, thereby absorbing electrolyte into the membrane and providing ion conductivity. The ionic conductivity increases as the monomer grafting rate increases. On the other hand, the membrane swells to contain the electrolyte in the pus.
Its dimensions change in length, width, thickness, and direction. The dimensional change due to this swelling droplet increases as the grafting ratio increases. The dimensional change of a membrane having ionic conductivity (electrical resistance) that can be used as a separator in a normal battery in an electrolytic solution is 15 to 20%, and reaches as much as 25%. Such a significant dimensional change, particularly in the vertical and horizontal directions, makes battery assembly extremely difficult in a small battery with limited dimensions and volume. Furthermore, even in large batteries where dimensional changes are relatively permissible, the separator sandwiched between the electrodes swells after electrolyte injection, creating uneven voids between the electrodes and causing gas retention, which impairs battery performance. There were drawbacks such as lowering the Conventionally, these grafted membranes have been developed to eliminate such drawbacks (in the pre-mechanically stretched state) and to provide the battery electrolyte with other separators that have dimensional stability (particularly in the longitudinal and transverse directions), such as cellophane, synthetic By pasting it with a porous film made of resin, swelling changes caused by the electrolyte were prevented. For this reason, the graft membrane has not been used alone, but in combination with other separators. Therefore, despite the excellent performance of graft membranes, graft membranes have not been effective in improving the performance of batteries, particularly in improving volumetric efficiency.
The present invention eliminates the above-mentioned drawbacks of the conventional art and provides a separator with particularly excellent dimensional stability.

すなわち、ポリエチレンフィルムを幹ポリマーとし、イ
オン交換基を有する単量体をグラフト重合させる際に、
グラフト率が低いか、または全くグラフトしてない部分
(以下これを非グラフ卜部と称する)を、グラフト率の
高い部分の周囲に連続して形成せしめて、グラフト率の
高い部分を不連続化し他の高グラフト率の部分と分離せ
しめるものである。このグラフト率の高い部分が不連続
したグラフト膜は、その部分のみが電解液に勝潤しても
、その周囲の非グラフ卜部は全〈膨潤しないかまたは極
めて低い膨潤のために、セパレータ全体としてはその寸
法変化は極めて少ないものとなる。すなわち、高グラフ
ト率の部分の周囲に、非グラフ卜部が配置しているため
に膜の膨潤は高グラフト率の部分だけで生じセパレータ
として使用されるときの寸法には影響を与えない。この
セパレータの電気抵抗は、フィルム全面に均一にグラフ
ト重合し、かつグラフト率を低く4して膨潤率を抑制し
たグラフト膜の電気抵抗よりも低い。グラフト膜におい
て一般に電気抵抗とグラフト率の関係は対数的比例関係
にあり、グラフト率の若干の低下は著しい電気抵抗の増
加をもたらす。本発明のセパレータの電気抵抗は、非グ
ラフ卜部と高グラフ卜部との比率によるため、平均グラ
フト率が低下しても電気抵抗は極端に増加することがな
い。この非グラフ卜部と高グラフ卜部の形成方法は、そ
のグラフト重合方法に応じて適当な方法を選ぶことがで
きる。グラフト重合法としては、■基材フィルムと単量
体の共存下で電離性放射線を照射してグラフト重合する
方法(同時照射法)、■あらかじめ基材フィルムに電離
性放射線を照射したのちに、単量体と薮触させるグラフ
ト重合法(前照射法)「■単量体と基村フィルムの共存
下で重合開始剤を用いるグラフト重合法(化学法)など
があり、これらのいずれの方法によっても本発明のセパ
レータを取得することが出釆る。すなわち、前照射法に
おいては、あらかじめポリエチレンフィルムに電離性放
射線を照射する際放射線を遮蔽する物質、例えば金属性
の網目状物を被照射フィルムの面上に当接して照射を行
なう。この金属網目状物にて遮蔽された部分は、放射線
の照射を受けないため、グラフト重合の開始点(主とし
てラジカル)が生成しないので単量体を接触させてもグ
ラフト重合は起らない。また他の方法としては、ポリエ
チレンと単量体とのグラフト重合を阻害する物質、例え
ば単量体溶液が水溶液の場合には油性インキなどをポリ
エチレンフィルムの表面上に格子状に印刷または塗布す
ることにより、この部分と単量体との接触を阻むことに
より、非グラフ卜部を形成せしめることが可能である。
同時照射法および化学法においても、上述と同様な方法
で適宜、単量体の種類、溶媒などを考慮して非グラフ卜
部を形成することができる。この高グラフ卜部および非
グラフ卜部の形状および大きさは、使用される電池に応
じて適宜選択することができる。
That is, when graft polymerizing a monomer having an ion exchange group using a polyethylene film as a backbone polymer,
A part with a low grafting ratio or no grafting at all (hereinafter referred to as a non-grafting part) is continuously formed around a part with a high grafting ratio, and the part with a high grafting ratio is made discontinuous. It separates it from the part with a high grafting rate. In a graft membrane with discontinuous areas with a high graft ratio, even if only that area is wetted by the electrolyte, the surrounding non-grafted area does not swell or has very low swelling, so the separator as a whole does not swell. The dimensional change will be extremely small. That is, since the non-grafted portion is arranged around the portion with a high grafting ratio, swelling of the membrane occurs only in the portion with a high grafting ratio, and does not affect the dimensions when used as a separator. The electrical resistance of this separator is lower than that of a graft film that is uniformly graft-polymerized over the entire surface of the film and that has a low graft ratio of 4 to suppress the swelling ratio. In a grafted film, the relationship between electrical resistance and grafting ratio is generally logarithmically proportional, and a slight decrease in the grafting ratio results in a significant increase in electrical resistance. Since the electrical resistance of the separator of the present invention depends on the ratio of the non-grafted portion to the highly graphed portion, the electrical resistance will not increase excessively even if the average grafting rate decreases. A suitable method for forming the non-grafted portion and the highly graphed portion can be selected depending on the graft polymerization method. Graft polymerization methods include: ■ Graft polymerization by irradiating ionizing radiation in the coexistence of the base film and monomer (simultaneous irradiation method); ■ After irradiating the base film with ionizing radiation in advance, There is a graft polymerization method (pre-irradiation method) in which the monomer is brought into contact with the monomer, and a graft polymerization method (chemical method) in which a polymerization initiator is used in the coexistence of the monomer and the Motomura film. In other words, in the pre-irradiation method, when a polyethylene film is irradiated with ionizing radiation, a material that shields the radiation, such as a metallic mesh, is applied to the irradiated film. Irradiation is carried out by contacting the surface of the metal mesh.Since the area shielded by the metal mesh is not irradiated with radiation, no starting points (mainly radicals) for graft polymerization are generated, so the monomers cannot be brought into contact with each other. Another method is to apply a substance that inhibits graft polymerization between polyethylene and the monomer, such as oil-based ink when the monomer solution is an aqueous solution, to the surface of the polyethylene film. It is possible to form a non-graphed area by printing or coating it in a lattice pattern on top to prevent contact between this area and the monomer.
In the simultaneous irradiation method and the chemical method, the non-graph portion can be formed by the same method as described above, taking into consideration the type of monomer, solvent, etc. as appropriate. The shape and size of the high graph area and the non-graph area can be appropriately selected depending on the battery used.

例えば密閉形小型電池のように、セパレータの寸法が直
径1仇吻前後のものについては、10仇hesh以下に
相当するような形状および大きさの格子状の非グラフト
部と、それに囲まれた高グラフ卜部とを有するグラフト
膜がセパレータとして適している。一方開放型のNi−
Cd電池のように、セパレータ寸法が縦12伽、横10
仇で使用されるやや大型の電池では、2meshに相当
する格子模様でも構わない。また、グラフ卜部および非
グラフ卜部の形状は、水玉状、亀甲状、格子状など如何
なる形状でもよいが、少なくとも非グラフ卜部は連続し
、グラフ卜部は互いに分離して非グラフ卜部によってそ
の周囲が囲まれていることが必要である。次に、実施例
にて具体的に説明するが、かかる説明により本発明は何
ら限定されるものではない。
For example, in the case of a sealed small battery, where the separator size is around 1 mm in diameter, there is a grid-like non-grafted part with a shape and size equivalent to 10 mm or less, and a height surrounded by the non-grafted part. Graft membranes having graph sections are suitable as separators. On the other hand, open type Ni-
Like CD batteries, the separator dimensions are 12cm long and 10cm wide.
For a slightly larger battery used by the enemy, a lattice pattern equivalent to 2 mesh may be used. Furthermore, the shapes of the graph section and the non-graph section may be any shape such as polka dot, hexagonal, or lattice, but at least the non-graph section is continuous, and the graph section is separated from each other and surrounded by the non-graph section. It is necessary that the Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited by such explanation.

実施例 1 腰厚25仏肌の低密度ポリエチレンフィルムに油性べィ
ントを15皿esh相当の格子状に印刷して、独立した
四角の非印刷部と連続した印刷部からなるようにした。
Example 1 Oil-based paint was printed on a low-density polyethylene film with a waist thickness of 25 mm in a grid pattern equivalent to 15 esh sheets, so that the film consisted of independent square non-printed areas and continuous printed areas.

このポリエチレンフィルムに電子線(加速電圧MeV、
加速電流&hA)を30Mrad照射した。ついで、あ
らかじめ窒素ガスにて溶存酸素を除去(0.1脚以下)
したアクリル酸50部、水50部、モール塩0.25%
からなる単量体水溶液に、この被照射フィルムを250
0にて5時間浸潰した。こうして得たグラフト膜を水洗
し、2.5%KOH水溶液に浸潰して90ooにて5分
間加熱しカリウム塩とした。得られたセパレータの平均
グラフト率65%であり、40%KOH水溶液中250
0にてloo0批交流法で測定した電気抵抗は85の○
・めであった。また、40%KOH中に100m×10
0肌の寸法で浸潰したセパレータの伸びは0.5の×0
.3肌であった。一方、油性ペイントを印刷しない通常
のポリエチレンフィルムを使用し、実施例1と同じ方法
で得たグラフト膜は、グラフト率75%、電気抵抗70
の○・塊、40%KOH中の伸び率は縦、横ともに15
%であった。実施例2 、 膜厚25仏のの高密度ポリエチレンフィルムの表面上に
5皿eshのステンレス製のネットをあてがい、液体窒
素で冷却下、電子線を2■地ad照射した。
This polyethylene film was coated with an electron beam (acceleration voltage MeV,
An accelerating current &hA) of 30 Mrad was applied. Then, remove dissolved oxygen in advance with nitrogen gas (less than 0.1 leg)
50 parts of acrylic acid, 50 parts of water, 0.25% Mohr's salt
This irradiated film was added to a monomer aqueous solution consisting of
0 for 5 hours. The graft membrane thus obtained was washed with water, immersed in a 2.5% KOH aqueous solution, and heated at 90 oo for 5 minutes to form a potassium salt. The average grafting rate of the obtained separator was 65%, and 250% in 40% KOH aqueous solution.
The electrical resistance measured by the loo0 cross-current method at 0 is 85○
・I met you. In addition, 100 m x 10 in 40% KOH
The elongation of the separator soaked with the dimension of 0 skin is 0.5 x 0
.. It was 3 skin. On the other hand, a graft film obtained in the same manner as in Example 1 using a regular polyethylene film that is not printed with oil-based paint has a grafting rate of 75% and an electrical resistance of 70%.
○・Lump, elongation rate in 40% KOH is 15 both vertically and horizontally.
%Met. Example 2 Five esh stainless steel nets were placed on the surface of a high-density polyethylene film with a film thickness of 25 mm, and the net was irradiated with an electron beam for 2 times on the ground while cooling with liquid nitrogen.

Claims (1)

【特許請求の範囲】 1 ポリエチレンフイルムに、イオン交換基を有する単
量体をグラフト重合させたグラフト膜からなり、該グラ
フト膜の表面においては、全くグラフトされていない部
分またはグラフト率の低い部分からなる連続した層によ
り、グラフト率の高い部分が非連続的に分割されて存在
することを特徴とする電池用セパレータ。 2 ポリエチレンフイルムの表面に、単量体のグラフト
反応を阻害する物質を印刷により塗布し、しかる後にイ
オン交換基を有する単量体をグラフト重合させることに
より、未印刷部分に非連続的にグラフトされた部分を形
成することを特徴とするグラフト率の高い部分が全くグ
ラフトされていない部分またはグラフト率の低い部分か
らなる連続した層により非連続的に分割されている電池
用セパレータの製造方法。 3 ポリエチレンフイルムの表面に網目状金属多孔板を
あてて該フイルムに電離性放射線を照射し、次いで照射
されたフイルムをイオン交換基を有する単量体と接触さ
せてグラフト重合を行なわせることを特徴とするグラフ
ト率の高い部分が全くグラフトされていない部分または
グラフト率の低い部分からなる連続した層により非連続
的に分割されている電池用セパレータの製造方法。
[Scope of Claims] 1. It consists of a graft membrane in which a monomer having an ion exchange group is graft-polymerized onto a polyethylene film, and on the surface of the graft membrane, there is a part that is not grafted at all or a part with a low grafting rate. 1. A battery separator characterized in that a portion with a high grafting rate is discontinuously divided into continuous layers. 2. A substance that inhibits the grafting reaction of monomers is coated on the surface of a polyethylene film by printing, and then a monomer having an ion exchange group is grafted onto the surface of the polyethylene film. 1. A method for producing a battery separator in which a portion with a high grafting rate is discontinuously divided by a continuous layer consisting of a portion with no grafting or a portion with a low grafting rate. 3. A mesh metal porous plate is placed on the surface of a polyethylene film, the film is irradiated with ionizing radiation, and then the irradiated film is brought into contact with a monomer having an ion exchange group to carry out graft polymerization. A method for producing a battery separator in which a portion with a high grafting rate is discontinuously divided into continuous layers consisting of a portion with no grafting or a portion with a low grafting rate.
JP54030691A 1979-03-16 1979-03-16 Battery separator and its manufacturing method Expired JPS6019624B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54030691A JPS6019624B2 (en) 1979-03-16 1979-03-16 Battery separator and its manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54030691A JPS6019624B2 (en) 1979-03-16 1979-03-16 Battery separator and its manufacturing method

Publications (2)

Publication Number Publication Date
JPS55122361A JPS55122361A (en) 1980-09-20
JPS6019624B2 true JPS6019624B2 (en) 1985-05-17

Family

ID=12310696

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54030691A Expired JPS6019624B2 (en) 1979-03-16 1979-03-16 Battery separator and its manufacturing method

Country Status (1)

Country Link
JP (1) JPS6019624B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2625842B1 (en) * 1988-01-07 1990-01-26 Accumulateurs Fixes METHOD FOR MANUFACTURING A SEPARATOR FOR AN ALKALINE ACCUMULATOR AND SEPARATOR OBTAINED

Also Published As

Publication number Publication date
JPS55122361A (en) 1980-09-20

Similar Documents

Publication Publication Date Title
EP0549670B1 (en) Polymer membrane
Ishigaki et al. Graft polymerization of acrylic acid onto polyethylene film by preirradiation method. I. Effects of preirradiation dose, monomer concentration, reaction temperature, and film thickness
US4339473A (en) Gamma radiation grafting process for preparing separator membranes for electrochemical cells
JP3066087B2 (en) Solid aqueous electrolyte, electrochemical cell using the same, and method for producing the same
JPH06509208A (en) Method for manufacturing polymer sheets
EP0014459B1 (en) Process for production of separators for use in cells
JP2013249510A (en) Diaphragm for alkaline water electrolysis
JPS6134515B2 (en)
US5075342A (en) Process for producing an ion exchange membrane by grafting non ion-selective monomers onto a ion exchange
EP3845606A1 (en) Hydrogel and uses therefor
US4923611A (en) Novel anion-exchange membrane
CN1128411A (en) Battery separator and battery containing same
US4287272A (en) Cell separator and cell
JPS6019624B2 (en) Battery separator and its manufacturing method
JP5893511B2 (en) Diaphragm for alkaline water electrolysis
US4539277A (en) Ion exchange membrane and process for producing the same
FI80482B (en) FOERFARANDE FOER FRAMSTAELLNING AV EN FAST POLYMER ELEKTROLYTSTRUKTUR GENOM ANVAENDNING AV EN VAETSKA ELLER ETT LOESNINGSMEDEL.
DE112006003185T5 (en) Process for producing electrodes for fuel cells and polymer electrolyte fuel cells with fuel cell electrodes
JPH06325749A (en) Electrolytic conductive polymer film
JPS638582B2 (en)
JPS62252067A (en) Composite separator for battery
JPH01186767A (en) battery
JPS5953663B2 (en) Manufacturing method for battery separators
RU2523464C2 (en) Method of manufacturing polymer ion-exchange membrane by radiation-chemical method
JP3101058B2 (en) Battery separator