JPH0261912A - Manufacture of solid electrolytic sheets - Google Patents

Manufacture of solid electrolytic sheets

Info

Publication number
JPH0261912A
JPH0261912A JP63211689A JP21168988A JPH0261912A JP H0261912 A JPH0261912 A JP H0261912A JP 63211689 A JP63211689 A JP 63211689A JP 21168988 A JP21168988 A JP 21168988A JP H0261912 A JPH0261912 A JP H0261912A
Authority
JP
Japan
Prior art keywords
powder
solid electrolyte
sheet
solid electrolytic
kneaded
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
JP63211689A
Other languages
Japanese (ja)
Other versions
JPH0787045B2 (en
Inventor
Tadashi Yasuda
直史 安田
Masaki Nagata
正樹 永田
Noriko Kanee
鐘江 範子
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.)
JSR Corp
Original Assignee
Japan Synthetic Rubber 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 Japan Synthetic Rubber Co Ltd filed Critical Japan Synthetic Rubber Co Ltd
Priority to JP63211689A priority Critical patent/JPH0787045B2/en
Publication of JPH0261912A publication Critical patent/JPH0261912A/en
Publication of JPH0787045B2 publication Critical patent/JPH0787045B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Conductive Materials (AREA)
  • Manufacturing Of Electric Cables (AREA)
  • Secondary Cells (AREA)

Abstract

PURPOSE:To improve precision of thickness, ionic conductivity, and display smoothness of a solid electrolytic sheet by kneading a solid electrolytic powder with specific grain size and content with an insulating polymer elastic body while milling the electrolytic powder so as to control the grain size and content of the electrolytic powder dispersed in the elastic body, forming the resulting mixture into a sheet, and drying the sheet. CONSTITUTION:A solid electrolytic powder of which 80wt.% and more has grain size 50mum and more, an insulating polymer elastic body, and a solvent are kneaded each other. At the same time, the solid electrolytic powder is milled so as to make 90wt.% and more of the powder have grain size 10mum and less and obtain a kneaded body in which the powder is dispersed. Then, the kneaded body is molded into a sheet and dried. As the solid electrolytic powder, a copper ion conductive or a silver ion conductive inorganic solid electrolytic powder such as KyRb1-yCu4I2-xCl3+x (Y=0-0.5; X=0.2-0.6), MAg4I5 (M stands for Rb or K) is used. To prepare the powder for usage, these electrolytic powders are recrystallized in chloric acid, vacuum-dried at room temperature, milled while using toluene as a dispersant, press-molded, and then heated at 130 deg.C in nitrogen flow.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は固体電解質シートの製造方法に関し、さらに詳
しくは固体マイクロ電池等に使用されるイオン導電性に
優れた固体電解質シートに関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for manufacturing a solid electrolyte sheet, and more particularly to a solid electrolyte sheet with excellent ionic conductivity used in solid micro batteries and the like.

[従来の技術] 電子産業における近年の技術的進歩は著しく、あらゆる
分野にIC,LSI等の電子部品が多く用いられている
が、電池技術の分野においても例外ではなく、製品の小
型化および薄型化が図られており、カード型電卓用電源
、カメラ用電源、腕時計用電源等として多量に使用され
ている。
[Prior Art] Technological advances in the electronics industry have been remarkable in recent years, and electronic components such as ICs and LSIs are now widely used in all fields.The field of battery technology is no exception, with products becoming smaller and thinner. It is widely used as power supplies for card-type calculators, cameras, wristwatches, etc.

これらの用途に用いられる電池は、アルカリ電池または
リチウム電池がほとんどであり、使用される電解質はい
ずれも液体電解質である。これら液体電解質を使用した
電池においては、電池の封口方法に高度の加工技術を要
し、現状ではガスケットを介したクリンプシールを用い
た封口技術が主に用いられている。
Most of the batteries used in these applications are alkaline batteries or lithium batteries, and the electrolytes used are liquid electrolytes. Batteries using these liquid electrolytes require advanced processing techniques to seal the batteries, and at present, sealing techniques using crimp seals using gaskets are mainly used.

しかし、電池が薄くなるほど封口部材の電池容積に占め
る割合が増大し、要求される電池容量の提供が離しくな
り、電池の薄型化にも限界がある。
However, as the battery becomes thinner, the ratio of the sealing member to the battery volume increases, making it more difficult to provide the required battery capacity, and there is a limit to how thin the battery can be made.

以上のことから、電池の薄型化および軽量化を図るため
に新しい電解質材料の開発が試みられており、−例とし
て易加工性、柔軟性等の長所を生かした高分子電解質の
電池等への応用がある。
Based on the above, attempts are being made to develop new electrolyte materials to make batteries thinner and lighter. For example, polymer electrolyte materials that take advantage of their advantages such as ease of processing and flexibility are being used for batteries. There are applications.

該高分子電解質のイオン伝導度は最も優れたものでも室
温で10’ s /cm程度であり、また移動イオンの
選択性が悪く、カチオン(例えばLi”)だけでなくア
ニオン(例えばC104)の移動を生ずる等の問題があ
り、実用段階に至っていない。
The ionic conductivity of the polymer electrolyte is about 10' s/cm at room temperature even if it is the best, and the selectivity of moving ions is poor, resulting in the movement of not only cations (for example, Li'') but also anions (for example, C104). However, it has not reached the stage of practical use due to problems such as the occurrence of

また大きなイオン伝導性を有する、例えば銀イオンや銅
イオン等のイオン伝導性固体電解質を利用する試みがな
されている。
Further, attempts have been made to utilize ion-conducting solid electrolytes having high ion conductivity, such as silver ions and copper ions.

これらの固体電解質は無機固体粉末であるため、電池等
への加工時に高圧プレスによるペレット化が必要となり
、得られるペレットは硬く、脆いため、固体電解質の電
気化学的特性を損なうことなく均一化および薄型化に限
界があり、大面積のものを得ることが困難である。
Since these solid electrolytes are inorganic solid powders, they must be pelletized by high-pressure press when processed into batteries, etc. The resulting pellets are hard and brittle, so it is difficult to homogenize and process them without impairing the electrochemical properties of the solid electrolytes. There is a limit to thinning, and it is difficult to obtain one with a large area.

さらに電池等に応用する場合、電極活物質との接合時に
、大きな加圧力で電解質−電極間を密着させる必要があ
るが、密着性等のバラつきの問題があり、かつ大面積で
の接合では均一な密着性が得られず、さらに固体電解質
の破壊を生ずるという問題もある。
Furthermore, when applied to batteries, etc., it is necessary to apply a large pressure to bring the electrolyte and electrode into close contact when bonding with the electrode active material, but there is a problem with variations in adhesion, and bonding over a large area is not uniform. There is also the problem that good adhesion cannot be obtained and furthermore, the solid electrolyte may be destroyed.

[発明が解決しようとする問題点コ 本発明の目的は、前記従来技術の問題点を解決し、イオ
ン伝導性、膜厚の均一性、表面平滑性、および電池とし
て使用する際の電極活物質との密着性に優れた薄型化お
よび大面積化が可能な固体電解質シートを提供すること
にある。
[Problems to be Solved by the Invention] The purpose of the present invention is to solve the problems of the prior art described above, and to improve ionic conductivity, uniformity of film thickness, surface smoothness, and improvement of electrode active materials when used as batteries. It is an object of the present invention to provide a solid electrolyte sheet that can be made thinner and larger in area and has excellent adhesion with other objects.

[問題点を解決するための手段] 本発明は、80重量%以上が50μm以上の粒径を有す
る固体電解質粉と絶縁性高分子弾性体(以下、単に「高
分子弾性体」という)と溶剤とを混練すると同時に固体
電解質粉を粉砕し、90重量%以上が10μm以下の粒
径を有する固体電解質粉が絶縁性高分子弾性体溶液中に
分散した混練物を調製し、該混練物をシート状に成形し
たのち乾燥することを特徴とする固体電解質シートの製
造方法を提供するものである。
[Means for Solving the Problems] The present invention provides a solid electrolyte powder in which 80% by weight or more has a particle size of 50 μm or more, an insulating polymeric elastomer (hereinafter simply referred to as "polymer elastomer"), and a solvent. At the same time, the solid electrolyte powder is pulverized to prepare a kneaded product in which 90% by weight or more of the solid electrolyte powder has a particle size of 10 μm or less dispersed in an insulating polymer elastomer solution, and the kneaded product is made into a sheet. The present invention provides a method for producing a solid electrolyte sheet, which is characterized by forming the solid electrolyte sheet into a shape and then drying it.

本発明に使用される固体電解質粉としては、例えばKy
Rb   Cu  I   C1(y:0t−y   
4 2−x   3+x 〜0.5、x:0,2〜o、6) 、MAg415(M
:RbまたはK)等の銅イオン伝導性の無機質固体電解
質粉または銀イオン伝導性の無機質固体電解質粉が挙げ
られ、イオン導電率が優れている点から、RbC−u 
 I   C1が4 2−x   3+x 好ましく、特にRbCu1C1が好ま 4 1.5  3.5 しい。KyRb   Cu  I   C1および1−
y   4 2−x   3+x MAg4I5はともに結晶性の物質[J、EIectr
ochem、 Soc、 L26.1858 (197
9)参照〕であり、例えばRbCu  I   C1は
次のようにして製4.2−x   3+x 造される。すなわち、CuC1およびCulを塩酸中で
再結晶させ、これらを室温で真空乾燥させ、一方、Rb
C1を100°Cで真空乾燥させ、これら成分塩を所定
量混合し、130℃で加熱して完全に脱水し、これをパ
イレックスガラス管中に真空封入し、加熱し融解させた
のち室温まで除冷し、固化したものをトルエンを分散剤
としてボールミルでよく粉砕し、粉砕した粉末を加圧成
型し、これを窒素気流中130℃で処理し、さらに再度
ボールミルで粉砕して粉体として得られる。
As the solid electrolyte powder used in the present invention, for example, Ky
Rb Cu I C1(y:0t-y
4 2-x 3+x ~0.5, x:0,2~o,6), MAg415 (M
:Rb or K), copper ion conductive inorganic solid electrolyte powder or silver ion conductive inorganic solid electrolyte powder.
I C1 is 4 2-x 3+x preferred, and RbCu1C1 is particularly preferred. KyRb Cu I C1 and 1-
y 4 2-x 3+x Both MAg4I5 are crystalline substances [J, EIectr
ochem, Soc, L26.1858 (197
9)], and for example, RbCu I C1 is manufactured as follows. That is, CuC1 and Cul were recrystallized in hydrochloric acid and dried under vacuum at room temperature, while Rb
C1 was vacuum dried at 100°C, a predetermined amount of these component salts were mixed, heated at 130°C to completely dehydrate it, vacuum sealed in a Pyrex glass tube, heated and melted, and then allowed to cool to room temperature. The cooled and solidified product is thoroughly ground in a ball mill using toluene as a dispersant, the ground powder is pressure molded, treated at 130°C in a nitrogen stream, and then ground again in a ball mill to obtain a powder. .

また本発明においては、80重量%以上が50μm以上
の粒径を有する固体電解質粉を用いる。
Further, in the present invention, solid electrolyte powder in which 80% by weight or more has a particle size of 50 μm or more is used.

該固体電解質粉が小さすぎると、みかけ比重が小さくな
り取り扱いにくくなる。また表面積が大きくなるために
保存時に劣化しやすく、シート化した場合のイオン導電
率が低下する。
If the solid electrolyte powder is too small, its apparent specific gravity will be low and it will be difficult to handle. In addition, since the surface area becomes large, it is easily deteriorated during storage, and when formed into a sheet, the ionic conductivity decreases.

本発明に使用される高分子弾性体としては、例えばスチ
レン−エチレン−ブチレン−スチレンブロック共重合体
(SEBS)、スチレン−エチレン−プロピレンブロッ
ク共重合体(SEP)、ポリエチレン、ポリプロピレン
、″ポリエチレンオキシド、ポリスチレン、塩化ビニル
、エチレン−酢酸エチル共重合体、1,4−ポリブタジ
ェン、天然ゴム、ポリイソプレン、SBRSNBRSE
PDM、EPM、ウレタンゴム、ポリエステル系ゴム、
クロロプレンゴム、エビクロルヒドリングム、ブチルゴ
ム、ホスファゼンゴム、1,2−ポリブタジェン、スチ
レン−ブタジェン−スチレンブロック共重合体(SBS
)、スチレン−イソプレン−スチレンブロック共重合体
(SIS)、およびこれらの混合物等が挙げられ、これ
らのうち、溶剤との溶解性、固体電解質粉との混練性、
電極活物質との接着性および得られる固体電解質シート
の強度の点から5EBS、SEPが好ましく、具体的に
は、5EBSとしてKratonG−1650、G−1
652、G−1657XSG−1660X、G−172
6(She 11社製)等が挙げられ、またSEPとし
て、Kraton  G−1701X、G−1702X
 (She 11社製)等が挙げられる。さらに柔軟性
の点から、ASTM硬度で90以下のものが好ましい。
Examples of the polymeric elastomer used in the present invention include styrene-ethylene-butylene-styrene block copolymer (SEBS), styrene-ethylene-propylene block copolymer (SEP), polyethylene, polypropylene, polyethylene oxide, Polystyrene, vinyl chloride, ethylene-ethyl acetate copolymer, 1,4-polybutadiene, natural rubber, polyisoprene, SBRSNBRSE
PDM, EPM, urethane rubber, polyester rubber,
Chloroprene rubber, shrimp chlorohydrin gum, butyl rubber, phosphazene rubber, 1,2-polybutadiene, styrene-butadiene-styrene block copolymer (SBS
), styrene-isoprene-styrene block copolymer (SIS), and mixtures thereof. Among these, solubility with solvents, kneadability with solid electrolyte powder,
From the viewpoint of adhesiveness with the electrode active material and strength of the solid electrolyte sheet obtained, 5EBS and SEP are preferable. Specifically, as 5EBS, Kraton G-1650, G-1
652, G-1657XSG-1660X, G-172
6 (manufactured by She 11), and as SEP, Kraton G-1701X, G-1702X
(manufactured by She 11). Furthermore, from the viewpoint of flexibility, it is preferable to have an ASTM hardness of 90 or less.

また固体電解質粉の耐熱性の点から、150℃以下での
成形加工性を存するものが好ましく、特に不飽和結合を
含まない高分子弾性体を50体積%以上含有するのが好
ましい。体積分率が50%未満の場合、得られる固体電
解質シートの分解電圧および電子輸率が悪化する場合が
ある。
In addition, from the viewpoint of heat resistance of the solid electrolyte powder, it is preferable that the solid electrolyte powder has moldability at 150° C. or lower, and it is particularly preferable that the solid electrolyte powder contains 50% by volume or more of an elastic polymer that does not contain unsaturated bonds. When the volume fraction is less than 50%, the decomposition voltage and electron transfer number of the obtained solid electrolyte sheet may deteriorate.

また溶剤としては、例えばn−ヘキサン、n −ヘプタ
ン、n−オクタン、シクロヘキサン、ベンゼン、トルエ
ン、キシレン、酢酸エチル、トリクレン等の非吸水性で
固体電解質粉と反応しない飽和炭化水素系溶剤、芳香族
炭化水素系溶剤、ハロゲン化炭化水素系溶剤またはエス
テル系溶剤が挙げられるが、これら溶剤の沸点が70〜
150°Cの範囲であることが好ましい。沸点が70’
C未満では、混合物をシート化する際、混合物中の溶剤
蒸発速度が速すぎるため均一で大面積のシートが得られ
ないことがあり、また沸点が150℃を超えると溶剤蒸
発速度が遅くなり生産効率が悪くなることがある。
Examples of solvents include saturated hydrocarbon solvents that do not absorb water and do not react with the solid electrolyte powder, such as n-hexane, n-heptane, n-octane, cyclohexane, benzene, toluene, xylene, ethyl acetate, and trichlene, and aromatic solvents. Examples include hydrocarbon solvents, halogenated hydrocarbon solvents, and ester solvents, and these solvents have a boiling point of 70 to
Preferably, the temperature is in the range of 150°C. boiling point is 70'
If the temperature is less than 150°C, the evaporation rate of the solvent in the mixture will be too fast and a uniform large-area sheet may not be obtained.If the boiling point exceeds 150°C, the evaporation rate of the solvent will be slow and production Efficiency may deteriorate.

本発明において、固体電解質粉を高分子弾性体中に均一
に分散させるためには、固体電解質粉および高分子弾性
体を溶剤を媒体として混合する。
In the present invention, in order to uniformly disperse the solid electrolyte powder in the elastomer polymer, the solid electrolyte powder and the elastomer polymer are mixed using a solvent as a medium.

この場合、固体電解質粉、高分子弾性体および溶剤の添
加順序は特に限定するものではないが、混合物の均一性
を高めるためには、高分子弾性体を前記溶剤に溶解させ
た溶液と固体電解質粉をボールミル、ペイントコンディ
ショナー、ホモジナイザー等で均一に混練すると同時に
固体電解質粉を粉砕する。
In this case, the order of addition of the solid electrolyte powder, the polymeric elastomer, and the solvent is not particularly limited, but in order to improve the uniformity of the mixture, a solution of the polymeric elastomer dissolved in the solvent and the solid electrolyte are added. The powder is uniformly kneaded using a ball mill, paint conditioner, homogenizer, etc., and at the same time the solid electrolyte powder is pulverized.

本発明において、混練後の固体電解質粉は90重量%以
上が10μm以下の粒径になるように粉砕される。混練
後の固体電解質粉の粒径が大きいと、得られる固体電解
質シートがイオン伝導性および表面平滑性の悪いものと
なる。前記のように粉砕された固体電解質粉を用いて得
られる固体電解質シートは、厚みが均一で表面平滑性に
優れ、かつピンホールのないものである。またイオン伝
導性も良好で、銅板等への接着性にも優れたものとなる
In the present invention, the solid electrolyte powder after kneading is pulverized so that 90% by weight or more has a particle size of 10 μm or less. If the particle size of the solid electrolyte powder after kneading is large, the obtained solid electrolyte sheet will have poor ionic conductivity and surface smoothness. A solid electrolyte sheet obtained using the solid electrolyte powder pulverized as described above has a uniform thickness, excellent surface smoothness, and no pinholes. It also has good ionic conductivity and excellent adhesion to copper plates and the like.

ここで、溶剤を含有する混練物の固形分重量濃度は50
〜80%が好ましい。固形分重量濃度が50%未満の場
合には、混練の際に剪断力が効率よく加わらず、また粘
度が低いために固体電解質シートの厚みを調整すること
が困難であり、80%を超える場合には混練が困難とな
る。
Here, the solid content weight concentration of the kneaded product containing the solvent is 50
~80% is preferred. If the solid content weight concentration is less than 50%, shearing force is not applied efficiently during kneading, and the viscosity is low, making it difficult to adjust the thickness of the solid electrolyte sheet, and if it exceeds 80%, This makes kneading difficult.

本発明において、固体電解質シートは前記にようにして
得られる溶剤を含有する混練物をシート状に成形したの
ち乾燥することにより得られるが、好ましくは前記のよ
うにして得られる溶剤を含有する混練物を非導電性網状
体の開口部に充填したのち乾燥する。この非導電性網状
体の材質とじては、例えばセルロース、ナイロン6、ナ
イロン66、ポリプロピレン、ポリエチレンポリエステ
ル、ガラス繊維等を挙げることができ、非導電性網状体
の具体例としては、これらの材質からなる織布または不
織布を挙げることができる。
In the present invention, the solid electrolyte sheet is obtained by forming the kneaded material containing the solvent obtained as described above into a sheet shape and then drying it, but preferably the kneaded material containing the solvent obtained as described above is dried. The material is filled into the openings of the non-conductive mesh and then dried. Examples of the material of this non-conductive network include cellulose, nylon 6, nylon 66, polypropylene, polyethylene polyester, glass fiber, etc. Specific examples of the non-conductive network include materials such as Examples include woven or nonwoven fabrics.

前記溶剤を含有する混練物を非導電性網状体の開口部に
充填する方法としては、溶剤を含有する混練物中に網状
体を含浸し、網状体に混練物を充分付着させたのち、硬
質ゴム、プラスチック、金属等からなるブレード、ロー
ル等により開口部に充填するとともに過剰に付着してい
る混練物を除去する方法が挙げられる。この際、ブレー
ド、ロール等と混練物の付着した網状体との間に、テフ
ロンシート、ポリエステルシート等を介在させ、過剰に
付着している混練物を除去してもよい。
The method for filling the openings of the non-conductive net with the kneaded material containing the solvent is to impregnate the net into the kneaded material containing the solvent, sufficiently adhere the kneaded material to the net, and then harden the kneaded material into the non-conductive mesh. Examples include a method of filling the opening with a blade, roll, or the like made of rubber, plastic, metal, etc., and removing excess adhering kneaded material. At this time, a Teflon sheet, a polyester sheet, etc. may be interposed between the blade, roll, etc. and the net-like body to which the kneaded material has adhered, and the excessively adhered kneaded material may be removed.

このようにして非導電性網状体の開口部に溶剤を含有す
る混練物を充填したのち、乾燥することにより固体電解
質シートが得られるが、混練工程、混練物の該網状体へ
の充填工程、および乾燥工程は相対湿度30%以下の環
境で行なうことが好ましい。相対湿度が30%を超える
と固体電解質粉の変質が生じることがある。相対湿度を
30%以下に保つ方法は特に限定されるものではなく、
脱湿した乾燥空気雰囲気、窒素、アルゴン等の不活性ガ
ス雰囲気で上記工程を行なえばよい。
In this way, a solid electrolyte sheet is obtained by filling the openings of the non-conductive network with a kneaded material containing a solvent and drying it. The drying step is preferably carried out in an environment with a relative humidity of 30% or less. If the relative humidity exceeds 30%, the quality of the solid electrolyte powder may change. The method of keeping the relative humidity below 30% is not particularly limited.
The above steps may be performed in a dehumidified dry air atmosphere or an inert gas atmosphere such as nitrogen or argon.

また非導電性網状体を用いた固体電解質シートは、導電
率および固体マイクロ電池等として使用する場合に用い
る電極活物質との密着性を向上させるためには、非導電
性網状体の上下に各5〜25μmの該混練物層を有する
ことが好ましく、該固体電解質シートの厚みは好ましく
は10〜250μmである。該シートの厚みが10μm
未満では裂けやすく強度が保てなくなり、厚みが250
μmを超えると導電率がI X 10’ s /cm以
下となりやすい。
In addition, in order to improve the conductivity and adhesion of a solid electrolyte sheet using a non-conductive network to the electrode active material used when used as a solid micro-battery, etc., it is necessary to It is preferable to have the kneaded material layer of 5 to 25 μm, and the thickness of the solid electrolyte sheet is preferably 10 to 250 μm. The thickness of the sheet is 10 μm
If the thickness is less than 250 mm, it will tear easily and will not maintain its strength.
If it exceeds μm, the conductivity tends to be less than I x 10' s/cm.

なお本発明において、固体電解質粉の固体電解質シート
中における体積分率は55〜95%であることが好まし
く、より好ましくは75〜92%である。固体電解質粉
の体積分率が55%未満の場合には混練物の導電率がI
 X 10’ s /cm以下となり実用に適さず、ま
た体積分率が95%を超えると得られる固体電解質シー
トが脆くなることがある。
In the present invention, the volume fraction of the solid electrolyte powder in the solid electrolyte sheet is preferably 55 to 95%, more preferably 75 to 92%. When the volume fraction of solid electrolyte powder is less than 55%, the conductivity of the kneaded material is I
If the volume fraction is less than X 10' s /cm, it is not suitable for practical use, and if the volume fraction exceeds 95%, the obtained solid electrolyte sheet may become brittle.

また本発明において、固体電解質シートの硬度は、好ま
しくはASTM−A硬度で65〜96である。該シート
の硬度が65未満では、固体電解質シートの導電率がI
 X 10’ s /cm以下となり、また硬度が96
を超えると固体電解質シートの可撓性が悪くなり脆くな
ることがある。
Further, in the present invention, the hardness of the solid electrolyte sheet is preferably 65 to 96 in terms of ASTM-A hardness. When the hardness of the sheet is less than 65, the conductivity of the solid electrolyte sheet is I
X 10's/cm or less, and the hardness is 96
If it exceeds this, the flexibility of the solid electrolyte sheet may deteriorate and it may become brittle.

さらに、本発明で得られる固体電解質シートは電極活物
質との接着強度を増すために、例えば混練物中に変性ロ
ジン、ロジン誘導体、テルペン樹脂、クマロン−インデ
ン樹脂、フェノール変性クマロン−インデン樹脂等のロ
ジン系粘着付与剤、芳香族系粘着付与剤またはテルペン
系粘着付与剤が添加されていてもよい。
Furthermore, the solid electrolyte sheet obtained according to the present invention contains, for example, modified rosin, rosin derivative, terpene resin, coumaron-indene resin, phenol-modified coumaron-indene resin, etc. in the kneaded material in order to increase the adhesive strength with the electrode active material. A rosin tackifier, an aromatic tackifier or a terpene tackifier may be added.

[実 施 例コ 以下、本発明を図面および実施例により詳細に説明する
が、本発明はこれら実施例に限定されるものではない。
[Example] Hereinafter, the present invention will be explained in detail with reference to drawings and examples, but the present invention is not limited to these examples.

第1図は本発明の固体電解質シートの製造方法を示す説
明図である。
FIG. 1 is an explanatory diagram showing the method for manufacturing a solid electrolyte sheet of the present invention.

第1図において、基材としての織布1はフィード=斗ロ
ール4により固体電解質粉と高分子弾性体と溶剤との混
練物2が入った処理溶液5に浸漬されたのち引き上げら
れ、ブレード3で織布の開口部に該混練物が充分に充填
されたのち、図示されていない乾燥装置で乾燥され固体
電解質シートが得られる。
In FIG. 1, a woven fabric 1 as a base material is dipped in a treatment solution 5 containing a kneaded material 2 of solid electrolyte powder, polymeric elastomer, and solvent by a feed roll 4, and then pulled up by a blade 3. After the kneaded material is sufficiently filled into the openings of the woven fabric, it is dried in a drying device (not shown) to obtain a solid electrolyte sheet.

実施例1 スチレン−エチレン−ブチレン−スチレンブロック共重
合体(以下Is E B SJと略す、シェル社製、商
品名Kraton  G−1650、比重二0.92)
とスチレン−ブタジェン−スチレンブロック共重合体(
以下rSBSJと略す、日本合成ゴム社製、TR−20
00、比重:0.96)とを体積比で8/2となるよう
に秤量し、これらをトルエン中に溶解させて溶液重量濃
度10%の高分子弾性体溶液を得た。これに粒径が60
μm以上の粒子を80重量%有するRbCu4■1.5
C】3.5固体電解質粉(比重:4.5)を50g加え
て混合し、固形分重量濃度が69%である混合物を得た
Example 1 Styrene-ethylene-butylene-styrene block copolymer (hereinafter abbreviated as Is E B SJ, manufactured by Shell, trade name Kraton G-1650, specific gravity 2 0.92)
and styrene-butadiene-styrene block copolymer (
TR-20, manufactured by Japan Synthetic Rubber Co., Ltd., hereinafter abbreviated as rSBSJ
00, specific gravity: 0.96) were weighed so that the volume ratio was 8/2, and these were dissolved in toluene to obtain a polymeric elastomer solution with a solution weight concentration of 10%. This has a particle size of 60
RbCu4■1.5 with 80% by weight of particles larger than μm
C] 50 g of 3.5 solid electrolyte powder (specific gravity: 4.5) was added and mixed to obtain a mixture having a solid content weight concentration of 69%.

得られた混合物をペイントコンディショナーにて2時間
混練し、第1図に示すような処理容器5に移した。
The resulting mixture was kneaded in a paint conditioner for 2 hours and transferred to a processing container 5 as shown in FIG.

次に厚み50μmのナイロン製織布を用い、この織布を
処理容器5内の混練物中に浸漬させ、織布の表面に混練
物を充分に付着させたのち、フッ素ゴム製のブレード3
で織布を挟み、充分な挟持力を加えつつ、織布をブレー
ド3より引張り出し、混練物を織布の開口部に充填した
。得られたシートを窒素気流中で充分に乾燥させ、混線
物中の溶剤を除去し、固体電解質シートを得た。得られ
た固体電解質シートの厚み、光沢、全導電率および銅板
への接着性、ならびに混練後の固体電解質粉の粒径が1
0μm以下の粒子の含有割合を下記の方法により測定し
、評価を行ない、その結果を表−1に示した。
Next, using a nylon woven fabric with a thickness of 50 μm, this woven fabric is immersed in the kneaded material in the processing container 5, and after the kneaded material is sufficiently adhered to the surface of the woven fabric, the fluororubber blade 3
While applying sufficient clamping force, the woven fabric was pulled out from the blade 3, and the kneaded material was filled into the openings of the woven fabric. The obtained sheet was sufficiently dried in a nitrogen stream to remove the solvent in the mixed material, and a solid electrolyte sheet was obtained. The thickness, gloss, total conductivity, and adhesion to the copper plate of the obtained solid electrolyte sheet, and the particle size of the solid electrolyte powder after kneading are 1.
The content ratio of particles of 0 μm or less was measured and evaluated by the following method, and the results are shown in Table 1.

厚み:ダイヤル厚みゲージ(尼崎製作所製)を用いて、
固体電解質シート(5mX0.225m)1枚について
100箇所の厚みを測定して、その平均を求めた。また
厚みの変動係数は、以下の式のように該平均の厚みの値
と各箇所の測定値との差の平均から求めた。
Thickness: Using a dial thickness gauge (manufactured by Amagasaki Seisakusho),
The thickness of one solid electrolyte sheet (5 m x 0.225 m) was measured at 100 locations, and the average thereof was determined. Further, the coefficient of variation in thickness was determined from the average of the differences between the average thickness value and the measured value at each location, as shown in the following equation.

標準偏差 変動係数(CV) −xloo (%)平均値 光沢ニゲロスメーターにて45°で測定した。standard deviation Coefficient of variation (CV) - xloo (%) average value Measured at 45° using a gloss Nigelosmeter.

全導電率:固体電解質シートを銅板間に挟み、130°
Cで10kg/crIの加圧を5分間行なって接着した
もので、交流I K11zでのインピーダンスをLCR
メーター(YHP4274A)で評価し、その直流成分
(6A)より求めた。
Total conductivity: solid electrolyte sheet sandwiched between copper plates, 130°
It was bonded by applying a pressure of 10 kg/crI for 5 minutes at C, and the impedance at AC I K11z was LCR.
It was evaluated using a meter (YHP4274A) and determined from its DC component (6A).

銅板への接着性:固体電解質シートを銅板間に挟み、1
30℃で10kg/cdの加圧を5分間行ない、銅板に
接着した固体電解質シートに対して基盤目テスト(市販
セロテープ、折目の大きさ=1mmX1mm、テスト回
数=100回ンを行ない評価した。
Adhesion to copper plates: sandwich the solid electrolyte sheet between copper plates,
A pressure of 10 kg/cd was applied at 30° C. for 5 minutes, and the solid electrolyte sheet adhered to the copper plate was subjected to a base grain test (commercial cellophane tape, fold size = 1 mm x 1 mm, number of tests = 100 times) for evaluation.

粒径10μm以下の粒子の含有割合:混練後の該混練物
を走査型電子顕微鏡(JSM−840)にて観察した。
Content ratio of particles with a particle size of 10 μm or less: The kneaded product after kneading was observed with a scanning electron microscope (JSM-840).

実施例2 実施例1において、混練物中の固体電解質粉の高分子弾
性体に対する体積分率を90%および固形分重量濃度を
79%とした以外は実施例1と同様にして固体電解質シ
ートを得、その特性を評価し、結果を表−1に示した。
Example 2 A solid electrolyte sheet was produced in the same manner as in Example 1, except that the volume fraction of the solid electrolyte powder in the kneaded material with respect to the polymer elastomer was 90% and the solid content weight concentration was 79%. The properties were evaluated and the results are shown in Table 1.

比較例1 実施例1において、高分子弾性体溶液重量濃度4%を用
い、混練物中の固体電解質粉の高分子弾性体に対する体
積分率を55%および固形分重量濃度を22%とし、ペ
イントコンディショナーによる混練を50分とした以外
は実施例1と同様にして固体電解質シートを得、その特
性を評価し、結果を表−1に示した。
Comparative Example 1 In Example 1, the weight concentration of the polymeric elastomer solution was 4%, the volume fraction of the solid electrolyte powder to the polymeric elastomer in the kneaded product was 55%, and the solid content weight concentration was 22%, and paint A solid electrolyte sheet was obtained in the same manner as in Example 1, except that the kneading with the conditioner was carried out for 50 minutes, and its properties were evaluated. The results are shown in Table 1.

比較例2 実施例1において、混練前の固体電解質粉の粒径が10
μm以下の粒子を90重量%以上有するものとした以外
は実施例1と同様にして固体電解質シートを得、その特
性を評価し、結果を表−1に示した。
Comparative Example 2 In Example 1, the particle size of the solid electrolyte powder before kneading was 10
A solid electrolyte sheet was obtained in the same manner as in Example 1 except that it contained 90% by weight or more of particles of .mu.m or less, and its properties were evaluated. The results are shown in Table 1.

以下余白 [発明の効果コ 本発明によれば、極めて厚み精度に優れ、イオン伝導性
が高く、かつ表面平滑性に優れた固体電解質シートを得
ることができる。また本発明で得られる固体電解質シー
トは、電池を製造する際の電極活物質との密着性に優れ
、薄型化および大面積化が図れるため従来困難とされて
きた、例えば1.0mm以下の厚さの固体マイクロ電池
用電解質シート、エレクトロクロミックデイスプレィ素
子、電気二重層キャパシタ等の電気化学素子材料として
有用である。
Margin below [Effects of the Invention According to the present invention, it is possible to obtain a solid electrolyte sheet with extremely excellent thickness accuracy, high ionic conductivity, and excellent surface smoothness. In addition, the solid electrolyte sheet obtained by the present invention has excellent adhesion with electrode active materials when manufacturing batteries, and can be made thinner and larger in area. It is useful as a material for electrochemical devices such as electrolyte sheets for solid-state microbatteries, electrochromic display devices, and electric double layer capacitors.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の固体電解質シートの製造方法を示す
説明図である。 1・・・・・・織  布   2・・・・・・混合溶液
3・・・・・・ブレード   4・・・・・・フィード
ロール5・・・・・・処理容器 5:処理容器 特許出願人  日本合成ゴム株式会社 手続補正書 1.事件の表示 特願昭63−211689号 2、発明の名称 固体電解質シートの製造方法 3、補正をする者 事件との関係  特許出願人 住 所  東京都中央区築地二丁目11番24号連絡先
  東京都中央区築地二丁目11番24号日本合成ゴム
株式会社 特許部 電話(03)541−4111■ 5、補正の内容 (1)明細書第9頁第8行と第9行の間に以下の文章を
追加する。 「なお、混練後の固体電解質粉の粒径は小さいほど、電
子伝導率が小さくなる。」 (2)同書第14頁第15行「全導電率および」を[全
導電率、電子伝導率および」と訂正する。 (3]  同書同頁第17行「10μm以下の粒子の含
有割合」を[10μm以下の粒子および1μm以下の粒
子の含有割合]と訂正する。 (4)回書第15頁下から第7行と下から第6行の間に
以下の文章を追加する。 [電子伝導率:固体電解質シートを白金板と銅板の間に
挟み、130℃で10kg/cJの加圧を5分間行なっ
て接着したもので、白金板側を正とし、銅板側を負とし
て、0.60Vの電圧を印加して一定電圧となるところ
の電流値より求めた。」 (5)同書第16頁第1行「粒径10μm以下の粒子の
含有割合」を[粒径10μm以下の粒子および1μm以
下の粒子の含有割合」と訂正する。 (6)伺書同頁第9行と第10行の間に以下の文章を追
加する。 [実施例3 実m例1において、得られた混合物をペイントコンディ
ショナーにて6時間混練した以外は実施例1と同様にし
て固体電解質シートを得、その特性を評価し、結果を表
−1に示した。」(7)同書第18頁「表−1」を別紙
の通りに訂正する。 以   上
FIG. 1 is an explanatory diagram showing the method for manufacturing a solid electrolyte sheet of the present invention. 1...Woven fabric 2...Mixed solution 3...Blade 4...Feed roll 5...Processing container 5: Processing container patent application Person Japan Synthetic Rubber Co., Ltd. Procedural Amendment 1. Display of the case Japanese Patent Application No. 63-211689 2, Name of the invention Method for manufacturing solid electrolyte sheet 3, Person making the amendment Relationship to the case Patent applicant address 2-11-24 Tsukiji, Chuo-ku, Tokyo Contact information Tokyo Japan Synthetic Rubber Co., Ltd. Patent Department, 2-11-24 Tsukiji, Chuo-ku, Tokyo Telephone: (03) 541-4111 ■ 5. Contents of amendment (1) The following statement must be made between lines 8 and 9 on page 9 of the specification. Add text. "The smaller the particle size of the solid electrolyte powder after kneading, the smaller the electronic conductivity." ” he corrected. (3) "Content ratio of particles of 10 μm or less" in line 17 of the same page of the same book is corrected to "content ratio of particles of 10 μm or less and particles of 1 μm or less". (4) Circular, page 15, line 7 from the bottom Add the following text between the 6th line from the bottom. [Electronic conductivity: A solid electrolyte sheet was sandwiched between a platinum plate and a copper plate, and the sheets were bonded together by applying a pressure of 10 kg/cJ at 130°C for 5 minutes. (5) P. 16, line 1 of the same book, "Grain "Content ratio of particles with a diameter of 10 μm or less" should be corrected to "Content ratio of particles with a diameter of 10 μm or less and particles with a diameter of 1 μm or less." (6) The following sentence should be added between lines 9 and 10 of the same page of the inquiry letter [Example 3] A solid electrolyte sheet was obtained in the same manner as in Example 1 except that the obtained mixture was kneaded in a paint conditioner for 6 hours, its properties were evaluated, and the results are presented. (7) "Table 1" on page 18 of the same book is corrected as shown in the attached sheet.

Claims (1)

【特許請求の範囲】[Claims]  80重量%以上が50μm以上の粒径を有する固体電
解質粉と絶縁性高分子弾性体と溶剤とを混練すると同時
に固体電解質粉を粉砕し、90重量%以上が10μm以
下の粒径を有する固体電解質粉が絶縁性高分子弾性体溶
液中に分散した混練物を調製し、該混練物をシート状に
成形したのち乾燥することを特徴とする固体電解質シー
トの製造方法。
A solid electrolyte powder in which 80% by weight or more has a particle size of 50 μm or more, an insulating polymer elastomer, and a solvent are kneaded and the solid electrolyte powder is simultaneously pulverized to produce a solid electrolyte in which 90% by weight or more has a particle size of 10 μm or less. A method for producing a solid electrolyte sheet, which comprises preparing a kneaded product in which powder is dispersed in an insulating polymer elastomer solution, forming the kneaded product into a sheet shape, and then drying the kneaded product.
JP63211689A 1988-08-26 1988-08-26 Method for manufacturing solid electrolyte sheet Expired - Lifetime JPH0787045B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63211689A JPH0787045B2 (en) 1988-08-26 1988-08-26 Method for manufacturing solid electrolyte sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63211689A JPH0787045B2 (en) 1988-08-26 1988-08-26 Method for manufacturing solid electrolyte sheet

Publications (2)

Publication Number Publication Date
JPH0261912A true JPH0261912A (en) 1990-03-01
JPH0787045B2 JPH0787045B2 (en) 1995-09-20

Family

ID=16609958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63211689A Expired - Lifetime JPH0787045B2 (en) 1988-08-26 1988-08-26 Method for manufacturing solid electrolyte sheet

Country Status (1)

Country Link
JP (1) JPH0787045B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999012221A1 (en) * 1997-09-03 1999-03-11 Matsushita Electric Industrial Co., Ltd. Solid electrolytic moldings, electrode moldings, and electrochemical elements
WO2007148805A1 (en) * 2006-06-21 2007-12-27 Toyota Jidosha Kabushiki Kaisha Methods of producing reinforced electrolyte membrane and membrane electrode joint body
JP2012243496A (en) * 2011-05-18 2012-12-10 Toyota Motor Corp Method for producing sulfide solid electrolyte material and sulfide solid electrolyte material

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020203042A1 (en) 2019-03-29 2020-10-08 Jsr株式会社 Binder for solid-state secondary battery, binder composition for solid-state secondary battery, slurry for solid-state secondary battery, solid electrolytic sheet for solid-state secondary battery, and production methods therefor, and solid-state secondary battery and production method therefor

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6378405A (en) * 1986-09-19 1988-04-08 松下電器産業株式会社 Anisotropic ion conductor

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6378405A (en) * 1986-09-19 1988-04-08 松下電器産業株式会社 Anisotropic ion conductor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999012221A1 (en) * 1997-09-03 1999-03-11 Matsushita Electric Industrial Co., Ltd. Solid electrolytic moldings, electrode moldings, and electrochemical elements
WO2007148805A1 (en) * 2006-06-21 2007-12-27 Toyota Jidosha Kabushiki Kaisha Methods of producing reinforced electrolyte membrane and membrane electrode joint body
JP2008004344A (en) * 2006-06-21 2008-01-10 Toyota Motor Corp Reinforcing electrolyte membrane and method for producing membrane electrode assembly
JP2012243496A (en) * 2011-05-18 2012-12-10 Toyota Motor Corp Method for producing sulfide solid electrolyte material and sulfide solid electrolyte material

Also Published As

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