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JPH0576138B2 - - Google Patents
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JPH0576138B2 - - Google Patents

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Publication number
JPH0576138B2
JPH0576138B2 JP62073728A JP7372887A JPH0576138B2 JP H0576138 B2 JPH0576138 B2 JP H0576138B2 JP 62073728 A JP62073728 A JP 62073728A JP 7372887 A JP7372887 A JP 7372887A JP H0576138 B2 JPH0576138 B2 JP H0576138B2
Authority
JP
Japan
Prior art keywords
solid electrolyte
sheet
powder
electrode sheet
battery
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 - Lifetime
Application number
JP62073728A
Other languages
Japanese (ja)
Other versions
JPS63239775A (en
Inventor
Masaki Nagata
Tadashi Yasuda
Shigeo Kondo
Tadashi Tonomura
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.)
Mitsubishi Chemical Corp
JSR Corp
Panasonic Holdings Corp
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
Japan Synthetic Rubber Co Ltd
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Synthetic Chemical Industry Co Ltd, Japan Synthetic Rubber Co Ltd, Matsushita Electric Industrial Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP62073728A priority Critical patent/JPS63239775A/en
Priority to US07/172,166 priority patent/US4810599A/en
Priority to DE3852412T priority patent/DE3852412T2/en
Priority to EP88104873A priority patent/EP0284104B1/en
Priority to KR1019880003331A priority patent/KR970004137B1/en
Publication of JPS63239775A publication Critical patent/JPS63239775A/en
Publication of JPH0576138B2 publication Critical patent/JPH0576138B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F1/00Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics
    • G02F1/01Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour 
    • G02F1/15Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on an electrochromic effect
    • G02F1/1514Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on an electrochromic effect characterised by the electrochromic material, e.g. by the electrodeposited material
    • G02F1/1523Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on an electrochromic effect characterised by the electrochromic material, e.g. by the electrodeposited material comprising inorganic material
    • G02F1/1525Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on an electrochromic effect characterised by the electrochromic material, e.g. by the electrodeposited material comprising inorganic material characterised by a particular ion transporting layer, e.g. electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/04Hybrid capacitors
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/54Electrolytes
    • H01G11/56Solid electrolytes, e.g. gels; Additives therein
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621Binders
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/14Cells with non-aqueous electrolyte
    • H01M6/18Cells with non-aqueous electrolyte with solid electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/14Cells with non-aqueous electrolyte
    • H01M6/18Cells with non-aqueous electrolyte with solid electrolyte
    • H01M6/181Cells with non-aqueous electrolyte with solid electrolyte with polymeric electrolytes
    • 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)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Power Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Nonlinear Science (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Optics & Photonics (AREA)
  • General Physics & Mathematics (AREA)
  • Manufacturing & Machinery (AREA)
  • Primary Cells (AREA)
  • Secondary Cells (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は固体電解質電池に関し、さらに詳しく
は製造し易い柔軟性のある多層構造の固体電解質
電池に関する。 〔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、小型
化、薄型化等が図られ、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。 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は、電池の封口方法に
高度の加工技術を必要とし、現在では、ガスケツ
トを介したクリンプシールを用いた封口技術が主
流であるが、電池が薄くなる程、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
を提供し難くなり、電池の薄型化に限界がある。 最近では、リチウム系の固体電解質を用いた電
池も市販されているが、活性な金属リチウムを負
極活物質として使用しているため、液体電解質電
池以上の信頼性の高い電池封口技術が必要とさ
れ、薄型化が困難であるのが現状である。 このような状況において、電池の小型化、薄型
化等のために、高いイオン導電性の固体電解質材
料が使用されつつあるが、これらの電解質材料を
用いて電池を製造する場合にはさらに電極材料も
取り扱いが容易で、電池組立の際の加工性、生産
性等にも優れていることが必要となる。 固体電解質材料に関しては、高分子電解質の応
用が試みられており、従来の代表的なものとして
はポリ(メタクリル酸オリゴキシエチレン)−ア
ルカリ金属塩系が挙げられる。しかしながら、そ
のイオン導電性は最も優れたものでも室温で10-5
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+)のみならずアニオン
(例えばClO4 -)の移動を生ずる等の問題があり、
実用段階に到つていない。さらにこの種の材料で
電池を作成する際、負極活物質として前記金属リ
チウムを使用する必要があり、電池組立の際の加
工性、生産性等の面で大きなメリツトが得られ難
い。 さらに最近では、大きなイオン導電性を有する
リチウムイオン伝導性固体電解質、プロトン伝導
性固体電解質、銀イオン伝導性固体電解質または
銅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。 リチウムイオン伝導性固体電解質の代表的なも
のには0.4LiSiO4−0.6Li3VO4、プロトン伝導性固
体電解質の代表的なものにはH3Mo12PO40
29H2OやH3W12PO40・29H2O、銀イオン伝導性
固体電解質の代表的なものにはRbAg4I5、また銅
イオン伝導性固体電解質の代表的なものには
RbCu4I1.5Cl3.5がある。しかしながら、これらの
固体電解質や電極活物質は無機固体粉末であるた
め、製造時に、高圧プレスによるペレツト化が必
要であり、生産性、均一性等を得る上で大きな障
害となつている。さらに得られるペレツトは硬く
て、脆いため、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。また電池を製造する
際、電極活物質との接合作業において大きな加圧
力で固体電解質と電極活物質を密着させる必要が
あり、作業性、密着性等のばらつきの問題があ
る。さらに大面積での接合を図る場合均一な密着
が得られず、また固体電解質の破壊を生ずる問題
がある。 〔発明が解決しようとする問題点〕 本発明の目的は、前記従来技術の問題点を解決
し、薄型化等を図ることができ、しかも電極材料
の取り扱いが容易で、電池組立の際の加工性およ
び生産性に優れた固体電解質電池を提供すること
にある。 〔問題点を解決するための手段〕 本発明の固体電解質電池は、イオン伝導性の無
機質固体電解質粉(以下、単に「固体電解質粉」
という)を絶縁性高分子弾性体中に55〜95%の体
積分率で含有させ分散せしめた電解質シートを、
電極活物質粉と無機質固体電解質粉との混合物を
絶縁性高分子弾性体中に75〜95%の体積分率で含
有させ分散せしめた負の電極シートと正の電極シ
ートとの間に積層し、該電極シートに引き出し電
極を積層してなることを特徴とする。 本発明において、前記電極シートは、電極活物
質粉と固体電解質粉との混合比を段階的に変化せ
しめて混合比の順に積層させ、かつ、電解質シー
トと組み合わせる際には、固体電解質粉の混合割
合の大きい電極シートが電解質シートと接するよ
うにして、引き出し電極とともに一体成型するこ
とが好ましい。 本発明の固体電解質電池は、基本的に電解質シ
ート(以下、SEシートと称する)、電極シートお
よび引き出し電極から構成され、引き出し電極、
正の電極シート、SEシート、負の電極シート、
引き出し電極の順に積み重ね(積み重ねの順は逆
でも良い)、これらを一体成型して得られる。一
体成型する方法は、特に限定されるものではない
が、例えば不活性ガス下、100〜150℃程度の温度
で数十秒〜10分間程度加熱し加圧する方法が挙げ
られている。加熱し加圧した後、不活性ガス下で
密着力を均一にするために1〜3時間程度熱処理
を行なつてもよい。このようにして得られた固体
電解質電池は製造し易く柔軟性を有し、薄型で、
大面積を有するものも得られる。 前記固体電解質電池は、さらに簡便な封止技
術、例えばエポキシ樹脂等による樹脂封止または
ポリエチレンフイルム、ポリプロピレンフイルム
等によるラミネート封止により実用に供される。 本発明に使用されるSEシートの固体電解質粉
としては、例えばRbCu4I2-xCl3+x(xは0.2〜0.6)、
MAg4I5(MはRbまたはK)等が挙げられるが、
イオン導電性が優れている点から、RbCu4I1.5
Cl3.5が最も好ましい。SEシート中の固体電解質
粉の体積分率は、55〜95%であることが必要であ
る。固体電解質粉の体積分率が55%未満の場合、
導電率1×10-6s/cm以下となり、実用に適さな
い。また体積分率が95%を超える場合は、シート
化の際、脆くなりシートとしての形状が保てなく
なる。 本発明に使用される電極シートの電極活物質粉
としては、例えばCuxTiS2、CuxZrS2
AgxTiS2、AgxZrS2、LixWO3、LixTiS2
WO3、V2O5、HWO5等の粉末が用いられるが、
xが0.05〜0.20程度のものが充放電特性の上から
好ましい。さらにはCu、Ag等の金属粉末が用い
られるが、過放電を防止する上から、Cuの粉末
を用いたときはCu2Sの粉末を、Agの粉末を用い
たときはAg2Sの粉末をそれぞれCu(または
Ag):Cu2S(またはAg2S)=8:2〜6.5:4.5
(重量比)の割合で加えることが好ましい。 また、電極シート中の電極活物質粉/固体電解
質粉の割合は1/4〜5/4(重量比)が好ましい。電
極活物質粉に固体電解質粉を加える理由は、電極
−電解質間の界面抵抗を低減し、界面における電
荷移動が容易に行なわれるようにするためであ
る。電極シート中における固体電解質粉と電極活
物質粉の体積分率は75〜95%であることが必要で
ある。体積分率が75%未満では、SEシート中の
固体電解質粉との接触効率が低下して、充分な電
池特性が得られず、体積分率が95%を超えるとシ
ート化の際脆くなりシートとしての形状が保てな
くなる。 本発明に使用される固体電解質粉および電極活
物質粉の形状ならびに粒径は特に限定されるもの
ではないが、絶縁性高分子弾性体との混合し易さ
等の点から、100〜200メツシユ(タイラー標準
篩)を通過するものが好ましい。 本発明に使用される絶縁性高分子弾性体として
は、1,4−ポリブタジエン、天然ゴム、ポリイ
ソプレン、SBR、NBR、EPDM、EPM、ウレ
タンゴム、ポリエステル系ゴム、クロロプレンゴ
ム、エピクロルヒドリンゴム、シリコーンゴム、
スチレン−ブタジエン−スチレンブロツク共重合
体(SBS)、スチレン−イソプレン−スチレンブ
ロツク共重合体(SIS)、スチレン−エチレン−
ブチレン−スチレン共重合体(SEBS)、ブチル
ゴム、ホスフアゼンゴム、ポリエチレン、ポリプ
ロピレン、ポリエチレンオキシド、ポリプロピレ
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、1,2−ポリブタジエ
ン、ポリメタクリル酸メチルおよびこれらの混合
物等を挙げることができるが、シート間相互間の
接着性や引き出し電極との良好な接着性を図る上
から、熱可塑性を有するものが好ましく、さらに
柔軟性を得る上からは、ASTM A硬度で95以下
のものが好ましい。また固体電解質粉の耐熱性の
点から150℃以下での成型加工性を有するものが
好ましい。 固体電解質粉、電極活物質粉等を絶縁性高分子
弾性体中に均一に分散させシート化する方法は、
特に限定されるものではないが、例えば、バンバ
リミキサーにて、絶縁性高分子弾性体と固体電解
質粉、電極活物質粉等とを混練し、得られた混合
物をロール圧延してシート化する方法、絶縁性高
分子弾性体を特定の溶剤に溶解させた高分子溶液
と固体電解質粉、電極活物質粉等とをボールミル
等で混練し、得られた混合物をアプリケーターバ
ー等で圧延し溶剤を乾燥することによりシートを
得る方法等が挙げられる。特に後者の方法は、
100μm以下の厚みムラの少ない薄膜が得られ易
いこと、混練時の発熱が少なく固体電解質粉の変
質および分解が起こり難いこと、さらに混練時に
大気との接触がほとんどなく、固体電解質粉の湿
気、酸素等による変質および分解が起き難く、周
囲の湿度、酸素等の状態を特に調節する必要がな
いことから製造方法として好ましい。この場合に
用いられる溶剤としては、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溶剤
を使用することが好ましく、この場合の絶縁性高
分子弾性体としては、前記溶剤に可溶な1,4−
ポリブタジエン、天然ゴム、ポリイソプレン、
SBR、NBR、SBS、SIS、SEBS、ブチルゴム、
ホスフアゼンゴム、ポリエチレンオキシド、ポリ
スチレン、1,2−ポリブタジエン等の使用は好
ましい。 前記SEシートおよび電極シートに含有される
固体電解質粉または絶縁性高分子弾性体は、共通
でも異なつたものでもよいが、成型体の均質性、
SEシートと電極シートとの接着性等の面から共
通のものを用いることが好ましい。また、前記
SEシートおよび電極シートの厚みは、各々10〜
250μmおよび20〜250μmが好ましい。 本発明に用いられる引き出し電極の材料は、特
に限定されるものではないが、電極シートとの接
着性の点から、銅系の電極シートの場合は銀薄板
が好適であるが、銅薄板にニツケルメツキもしく
は金メツキを施したもの、またはリン青銅等の合
金でもよい。 本発明において電極シートは、SEシートと接
する面から固体電解質粉と電極活物質粉との混合
比を段階的に変化せしめ、SEシートと接する面
で固体電解質粉の比率が大きく、引き出し電極に
近づくに従い、固体電解質粉の比率が小さくなる
ように複数のシートが混合比の順に積層され多層
化された電極シートとすることが好ましい。この
場合の電極シートの多層化の程度は、特に限定さ
れるものではなく2層でも効果を有するが、好ま
しくは3〜9層である。ただし加工の煩雑さや厚
型化を避ける意味から3〜6層が適当である。こ
のように電極シートを多層化することにより、電
極−電解質間の界面抵抗を低減し、電流容量を大
きくする効果が得られる。 〔実施例〕 以下、本発明を実施例により説明するが、本発
明はこれらに限定されるものではない。 (実施例 1) 絶縁性高分子弾性体としてスチレン−ブタジエ
ン−スチレンブロツク共重合体(比重:0.96、日
本合成ゴム社製、TR−2000)1部(重量部、以
下同じ)をトルエン中に溶解させ高分子溶液を
得、これに4.2部の粒径200メツシユ以下のRbCu4
I1.5Cl3.5からなる固体電解質粉(比重:4.5)を加
えてボールミルにて2時間混練し、得られた混合
物をテフロンシート上でアプリケーターバーにて
引き延ばし乾燥空気中にてトルエンを蒸発させ、
体積分率90%、厚み20μmのSEシートを得た。 次にCuの粉末、Cu2Sの粉末およびRbCu4I1.5
Cl3.5からなる固体電解質粉を重量比でCu:Cu2
S:RbCu4I1.5Cl3.5=2.9:2.7:1の割合で混合
し、ペレツト状にプレス成型した後、ガラス管に
真空封入し200℃で17時間加熱し、このペレツト
を200メツシユ以下の粉末に粉砕して負極用粉末
を得た。この負極用粉末と前記スチレン−ブタジ
エン−スチレンブロツク共重合体とを前記SEシ
ート作成の場合と同様の方法で混練し、成型し、
体積分率90%、厚み45μmの負極シートを得た。 また、Cuの粉末とTiS2の粉末をモル比で
0.15:1の割合で混合してペレツト状にプレス成
型し、石英管に真空封入して550℃で72時間加熱
し、得られたCu0.15TiS2ペレツトを200メツシユ
以下となるように粉砕し、この粉末とRbCu4I1.5
Cl3.5からなる固体電解質粉を重量比で1:1に混
合し、正極用粉末を得た。この正極用粉末と上記
スチレン−ブタジエン−スチレン共重合体とを前
記SEシート作成の場合と同様の方法で混練し、
成型し、体積分率90%、厚み45μmの負極シート
を得た。 得られた正極シート、SEシート、負極シート
を順に積層し、引き出し電極に銅薄板を用いて
130℃でプレス成型し、周辺部をエポキシ樹脂で
封止し、電池を作成した。 第1図に得られた電池の断面図を示した。図
中、1はSEシート、2は正極シート、3は負極
シート、4および5は引き出し電極、6は封止材
である。得られた電池の厚みおよび全導電率、自
己放電特性、充放電サイクル、低温特性の試験結
果を第1表に示した。 なお、前記全導電率(s/cm)は、交流1KHz
でのインピーダンスをLCRメーター(横河ヒユ
ーレツトパツカード社製、YHP4274A)で評価
し、その直流成分より求めた。 自己放電特性は、4mAh/c.c.の充放電サイクル
(2時間放電、1時間充電)での電池電圧の変化
より求めた。 充放電サイクルは、2.5mAh/c.c.の充放電サイ
クルで、放電電圧ガ0.35ボルト以下になるサイク
ル数で示した。 低温特性は、−10℃における充放電特性で示し
た。 (実施例 2) 実施例1と同様の方法でSEシート(体積分率
90%および厚み20μm)を作成した。負極シート
(体積分率90%)として、Cuの粉末、Cu2Sの粉
末およびRbCu4I1.5Cl3.5からなる固体電解質粉末
を重量比でCu:Cu2S:RbCu4I1.5Cl3.5=3:
2:3(負極シート1;厚み20μm)、3:2:2
(負極シート2;厚み30μm)および3:2:1
(負極シート3;厚み30μm)の割合で混合した
ものをそれぞれ実施例1と同様の方法で作成し
た。また正極シート(体積分率90%)として、
Cu0.15TiS2の粉末とRbCu4I1.5Cl3.5からなる固体電
解質粉を重量比でCu0.15TiS2:RbCu4I1.5Cl3.5
1:3(正極シート1;厚み20μm)、1:2(正
極シート2;厚み30μm)および1:1(正極シ
ート3;厚み20μm)の割合で混合したものをそ
れぞれ実施例1と同様の方法で作成した。 得られたシートを正極シート3/正極シート
2/正極シート1/SEシート/負極シート1/
負極シート2/負極シート3の順で積層し、引き
出し電極に銅薄板を用い、実施例1と同様の方法
で電池を作成した。第2図に得られた電池の断面
図を示した。図中、2aは正極シート1,2bは
正極シート2,2cは正極シート3,3aは負極
シート1,3bは負極シート2,3cは負極シー
ト3である。得られた電池の実施例1と同様に試
験結果を第1表に示した。
[Industrial Application Field] The present invention relates to a solid electrolyte battery, and more particularly to a solid electrolyte battery having a flexible multilayer structure that is easy to manufacture. [Conventional technology] Recent technological advances in the electronics industry have been remarkable.
Electronic components such as ICs and LSIs are widely used in all fields, but even in the field of battery technology, efforts are being made to make them smaller and thinner, and they are now being used as power supplies for card-type calculators, cameras, wristwatches, etc. Used in large quantities. 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 technology to seal the battery, and currently the mainstream sealing technology uses crimp seals via gaskets, but the thinner the battery, the more difficult it is to use the sealing material. This increases the proportion of the battery's volume in the battery, making it difficult to provide the required battery capacity, and there is a limit to how thin the battery can be made. Batteries using lithium-based solid electrolytes have recently become commercially available, but since active metal lithium is used as the negative electrode active material, more reliable battery sealing technology than liquid electrolyte batteries is required. At present, it is difficult to make the device thinner. Under these circumstances, solid electrolyte materials with high ionic conductivity are being used to make batteries smaller and thinner, but when manufacturing batteries using these electrolyte materials, electrode materials are also required. It also needs to be easy to handle and have excellent workability and productivity during battery assembly. Regarding solid electrolyte materials, attempts have been made to apply polymer electrolytes, and a typical example of the conventional material is poly(oligoxyethylene methacrylate)-alkali metal salt system. However, even the best ionic conductivity is 10 -5 at room temperature.
s/cm, and the selectivity of moving ions is poor, causing problems such as the movement of not only cations (e.g. Li + ) but also anions (e.g. ClO 4 - ).
It has not reached the practical stage. Furthermore, when making a battery using this type of material, it is necessary to use the metal lithium as the negative electrode active material, and it is difficult to obtain significant benefits in terms of processability, productivity, etc. during battery assembly. More recently, attempts have been made to utilize lithium ion conductive solid electrolytes, proton conductive solid electrolytes, silver ion conductive solid electrolytes, or copper ion conductive solid electrolytes that have high ionic conductivity. A typical lithium ion conductive solid electrolyte is 0.4LiSiO 4 −0.6Li 3 VO 4 , and a typical proton conductive solid electrolyte is H 3 Mo 12 PO 40 .
29H 2 O, H 3 W 12 PO 40・29H 2 O, RbAg 4 I 5 is a typical silver ion conductive solid electrolyte, and RbAg 4 I 5 is a typical copper ion conductive solid electrolyte.
There is RbCu 4 I 1.5 Cl 3.5 . However, since these solid electrolytes and electrode active materials are inorganic solid powders, it is necessary to pelletize them using a high-pressure press during production, which is a major obstacle in achieving productivity, uniformity, etc. Furthermore, the resulting pellets are hard and brittle, so there is a limit to how thin they can be made, and it is difficult to obtain pellets with a large area. Furthermore, when manufacturing a battery, it is necessary to bring the solid electrolyte and electrode active material into close contact with each other using a large pressure during the bonding operation with the electrode active material, which causes problems with variations in workability, adhesion, and the like. Furthermore, when attempting to bond over a large area, there is a problem that uniform adhesion cannot be obtained and the solid electrolyte may be destroyed. [Problems to be Solved by the Invention] An object of the present invention is to solve the problems of the prior art as described above, to achieve thinning, etc., and to facilitate the handling of electrode materials, which facilitates processing during battery assembly. The object of the present invention is to provide a solid electrolyte battery with excellent performance and productivity. [Means for Solving the Problems] The solid electrolyte battery of the present invention uses ionically conductive inorganic solid electrolyte powder (hereinafter simply referred to as "solid electrolyte powder").
) is dispersed in an insulating polymeric elastomer at a volume fraction of 55 to 95%.
Laminated between a negative electrode sheet and a positive electrode sheet in which a mixture of electrode active material powder and inorganic solid electrolyte powder is contained and dispersed in an insulating polymeric elastomer at a volume fraction of 75 to 95%. , characterized in that an extraction electrode is laminated on the electrode sheet. In the present invention, the electrode sheet is laminated in the order of the mixing ratio by changing the mixing ratio of the electrode active material powder and the solid electrolyte powder in stages, and when combined with the electrolyte sheet, the mixing ratio of the electrode active material powder and the solid electrolyte powder is changed in stages. It is preferable to integrally mold the electrode sheet with the extraction electrode so that a large proportion of the electrode sheet is in contact with the electrolyte sheet. The solid electrolyte battery of the present invention basically consists of an electrolyte sheet (hereinafter referred to as SE sheet), an electrode sheet, and an extraction electrode.
Positive electrode sheet, SE sheet, negative electrode sheet,
It is obtained by stacking the extraction electrodes in this order (the order of stacking may be reversed) and molding them together. The method of integral molding is not particularly limited, but for example, a method of heating and pressurizing at a temperature of about 100 to 150° C. for several tens of seconds to about 10 minutes under an inert gas is mentioned. After heating and pressurizing, heat treatment may be performed for about 1 to 3 hours under an inert gas to make the adhesion uniform. The solid electrolyte battery thus obtained is easy to manufacture, flexible, thin, and
Large areas can also be obtained. The solid electrolyte battery is put to practical use by simpler sealing techniques, such as resin sealing with epoxy resin or the like, or lamination sealing with polyethylene film, polypropylene film, or the like. The solid electrolyte powder of the SE sheet used in the present invention includes, for example, RbCu 4 I 2-x Cl 3+x (x is 0.2 to 0.6),
Examples include MAg 4 I 5 (M is Rb or K),
RbCu 4 I 1.5 due to its excellent ionic conductivity
Cl 3.5 is most preferred. The volume fraction of solid electrolyte powder in the SE sheet needs to be 55 to 95%. If the volume fraction of solid electrolyte powder is less than 55%,
The conductivity is less than 1×10 -6 s/cm, making it unsuitable for practical use. Further, if the volume fraction exceeds 95%, the sheet becomes brittle and cannot maintain its shape when formed into a sheet. Examples of the electrode active material powder of the electrode sheet used in the present invention include CuxTiS 2 , CuxZrS 2 ,
AgxTiS 2 , AgxZrS 2 , LixWO 3 , LixTiS 2 ,
Powders such as WO 3 , V 2 O 5 and HWO 5 are used, but
It is preferable that x is about 0.05 to 0.20 from the viewpoint of charge/discharge characteristics. Furthermore, metal powders such as Cu and Ag are used, but in order to prevent overdischarge, Cu 2 S powder is used when Cu powder is used, and Ag 2 S powder is used when Ag powder is used. respectively Cu (or
Ag): Cu 2 S (or Ag 2 S) = 8:2 to 6.5:4.5
It is preferable to add at a ratio of (weight ratio). Moreover, the ratio of electrode active material powder/solid electrolyte powder in the electrode sheet is preferably 1/4 to 5/4 (weight ratio). The reason why the solid electrolyte powder is added to the electrode active material powder is to reduce the interfacial resistance between the electrode and the electrolyte and to facilitate charge transfer at the interface. The volume fraction of the solid electrolyte powder and the electrode active material powder in the electrode sheet needs to be 75 to 95%. If the volume fraction is less than 75%, the contact efficiency with the solid electrolyte powder in the SE sheet will decrease, making it impossible to obtain sufficient battery characteristics, and if the volume fraction exceeds 95%, the sheet will become brittle when formed into a sheet. It will no longer be able to maintain its shape. The shape and particle size of the solid electrolyte powder and electrode active material powder used in the present invention are not particularly limited, but from the viewpoint of ease of mixing with the insulating polymer elastomer, etc. (Tyler standard sieve) is preferred. Examples of the insulating polymer elastomer used in the present invention include 1,4-polybutadiene, natural rubber, polyisoprene, SBR, NBR, EPDM, EPM, urethane rubber, polyester rubber, chloroprene rubber, epichlorohydrin rubber, and silicone rubber. ,
Styrene-butadiene-styrene block copolymer (SBS), styrene-isoprene-styrene block copolymer (SIS), styrene-ethylene-
Butylene-styrene copolymer (SEBS), butyl rubber, phosphazene rubber, polyethylene, polypropylene, polyethylene oxide, polypropylene oxide, polystyrene, vinyl chloride, ethylene-ethyl acetate copolymer, 1,2-polybutadiene, polymethyl methacrylate, and these Examples include mixtures, but from the viewpoint of good adhesion between the sheets and good adhesion with the lead-out electrode, thermoplastic materials are preferable, and from the viewpoint of obtaining further flexibility, materials with ASTM A hardness are preferred. 95 or less is preferable. 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. The method of uniformly dispersing solid electrolyte powder, electrode active material powder, etc. in an insulating polymer elastomer and forming a sheet is as follows.
Although not particularly limited, for example, a method of kneading an insulating polymer elastomer, solid electrolyte powder, electrode active material powder, etc. in a Banbury mixer, and rolling the resulting mixture into a sheet. , a polymer solution in which an insulating polymer elastomer is dissolved in a specific solvent, solid electrolyte powder, electrode active material powder, etc. are kneaded in a ball mill, etc., and the resulting mixture is rolled with an applicator bar, etc., and the solvent is dried. Examples include a method of obtaining a sheet by doing so. In particular, the latter method
It is easy to obtain a thin film with a uniform thickness of 100 μm or less, there is little heat generation during kneading, and deterioration and decomposition of the solid electrolyte powder is difficult to occur.Furthermore, there is almost no contact with the atmosphere during kneading, and the solid electrolyte powder is free from moisture and oxygen. It is preferable as a manufacturing method because it is difficult to cause deterioration and decomposition due to etc., and there is no need to particularly adjust the surrounding humidity, oxygen, etc. conditions. In this case, use a non-water-absorbing solvent that does not react with the solid electrolyte powder, such as n-hexane, n-heptane, n-octane, cyclohexane, benzene, toluene, xylene, ethyl acetate, trichlene, etc. is preferable, and in this case, the insulating polymer elastomer is a 1,4-
polybutadiene, natural rubber, polyisoprene,
SBR, NBR, SBS, SIS, SEBS, butyl rubber,
The use of phosphazene rubber, polyethylene oxide, polystyrene, 1,2-polybutadiene, etc. is preferred. The solid electrolyte powder or insulating polymer elastomer contained in the SE sheet and the electrode sheet may be common or different, but the homogeneity of the molded body,
It is preferable to use a common material between the SE sheet and the electrode sheet from the viewpoint of adhesion between the SE sheet and the electrode sheet. Also, the above
The thickness of SE sheet and electrode sheet is 10~
250 μm and 20-250 μm are preferred. The material of the extraction electrode used in the present invention is not particularly limited, but from the viewpoint of adhesion with the electrode sheet, a thin silver plate is suitable for a copper-based electrode sheet, but a thin copper plate with nickel plating is preferable. Alternatively, it may be plated with gold or an alloy such as phosphor bronze. In the present invention, the electrode sheet gradually changes the mixing ratio of solid electrolyte powder and electrode active material powder from the surface in contact with the SE sheet, and the ratio of solid electrolyte powder is large on the surface in contact with the SE sheet, which approaches the extraction electrode. Accordingly, it is preferable to form a multilayered electrode sheet in which a plurality of sheets are laminated in order of mixing ratio so that the ratio of solid electrolyte powder becomes small. The degree of multilayering of the electrode sheet in this case is not particularly limited, and even two layers can have an effect, but preferably three to nine layers. However, from the viewpoint of avoiding complicated processing and thickening, it is appropriate to have 3 to 6 layers. By multilayering the electrode sheet in this manner, it is possible to reduce the interfacial resistance between the electrode and the electrolyte and increase the current capacity. [Example] The present invention will be described below with reference to Examples, but the present invention is not limited thereto. (Example 1) 1 part (parts by weight, same hereinafter) of styrene-butadiene-styrene block copolymer (specific gravity: 0.96, manufactured by Japan Synthetic Rubber Co., Ltd., TR-2000) as an insulating polymeric elastomer was dissolved in toluene. A polymer solution was obtained, and 4.2 parts of RbCu 4 with a particle size of 200 mesh or less was added to this.
A solid electrolyte powder (specific gravity: 4.5) consisting of I 1.5 Cl 3.5 was added and kneaded in a ball mill for 2 hours, the resulting mixture was spread on a Teflon sheet with an applicator bar, and the toluene was evaporated in dry air.
An SE sheet with a volume fraction of 90% and a thickness of 20 μm was obtained. Then Cu powder, Cu 2 S powder and RbCu 4 I 1.5
Solid electrolyte powder consisting of Cl 3.5 in weight ratio Cu:Cu 2
S:RbCu 4 I 1.5 Cl 3.5 = 2.9:2.7:1 ratio was mixed, press-molded into pellets, vacuum sealed in a glass tube and heated at 200℃ for 17 hours, and the pellets were made into powder of 200 mesh or less. The powder was pulverized to obtain a powder for negative electrode. This negative electrode powder and the styrene-butadiene-styrene block copolymer are kneaded and molded in the same manner as in the SE sheet production,
A negative electrode sheet with a volume fraction of 90% and a thickness of 45 μm was obtained. In addition, the molar ratio of Cu powder and TiS 2 powder is
The mixture was mixed at a ratio of 0.15:1, press-molded into pellets, vacuum sealed in a quartz tube, heated at 550°C for 72 hours, and the resulting Cu 0.15 TiS 2 pellets were crushed to a size of 200 meshes or less. This powder and RbCu 4 I 1.5
Solid electrolyte powder consisting of Cl 3.5 was mixed at a weight ratio of 1:1 to obtain a positive electrode powder. This positive electrode powder and the above styrene-butadiene-styrene copolymer are kneaded in the same manner as in the case of preparing the SE sheet,
A negative electrode sheet having a volume fraction of 90% and a thickness of 45 μm was obtained by molding. The obtained positive electrode sheet, SE sheet, and negative electrode sheet were laminated in order, and a copper thin plate was used as the extraction electrode.
A battery was created by press molding at 130°C and sealing the periphery with epoxy resin. FIG. 1 shows a cross-sectional view of the obtained battery. In the figure, 1 is an SE sheet, 2 is a positive electrode sheet, 3 is a negative electrode sheet, 4 and 5 are extraction electrodes, and 6 is a sealing material. Table 1 shows the test results for the thickness, total conductivity, self-discharge characteristics, charge/discharge cycle, and low-temperature characteristics of the obtained battery. In addition, the above-mentioned total conductivity (s/cm) is AC 1KHz.
The impedance was evaluated using an LCR meter (YHP4274A, manufactured by Yokogawa Heuretsu Pats Card Co., Ltd.), and was determined from the DC component. The self-discharge characteristics were determined from the change in battery voltage during a charge/discharge cycle of 4 mAh/cc (discharged for 2 hours, charged for 1 hour). The charge/discharge cycle is a charge/discharge cycle of 2.5 mAh/cc, and is expressed as the number of cycles at which the discharge voltage becomes 0.35 volt or less. Low-temperature characteristics were shown as charge-discharge characteristics at -10°C. (Example 2) SE sheet (volume fraction
90% and thickness 20 μm). As a negative electrode sheet (volume fraction 90%), solid electrolyte powder consisting of Cu powder, Cu 2 S powder, and RbCu 4 I 1.5 Cl 3.5 was used at a weight ratio of Cu:Cu 2 S:RbCu 4 I 1.5 Cl 3.5 = 3. :
2:3 (negative electrode sheet 1; thickness 20 μm), 3:2:2
(Negative electrode sheet 2; thickness 30μm) and 3:2:1
(Negative electrode sheet 3; thickness 30 μm) were prepared in the same manner as in Example 1. Also, as a positive electrode sheet (volume fraction 90%),
The weight ratio of solid electrolyte powder consisting of Cu 0.15 TiS 2 powder and RbCu 4 I 1.5 Cl 3.5 is Cu 0.15 TiS 2 :RbCu 4 I 1.5 Cl 3.5 =
Mixtures at a ratio of 1:3 (positive electrode sheet 1; thickness 20 μm), 1:2 (positive electrode sheet 2; thickness 30 μm), and 1:1 (positive electrode sheet 3; thickness 20 μm) were prepared in the same manner as in Example 1, respectively. Created with. The obtained sheets were divided into positive electrode sheet 3 / positive electrode sheet 2 / positive electrode sheet 1 / SE sheet / negative electrode sheet 1 /
A battery was produced in the same manner as in Example 1 by laminating negative electrode sheet 2/negative electrode sheet 3 in this order and using a thin copper plate as the lead electrode. FIG. 2 shows a cross-sectional view of the obtained battery. In the figure, 2a is a positive electrode sheet 1, 2b is a positive electrode sheet 2, 2c is a positive electrode sheet 3, 3a is a negative electrode sheet 1, 3b is a negative electrode sheet 2, and 3c is a negative electrode sheet 3. The test results of the obtained battery are shown in Table 1 in the same manner as in Example 1.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

本発明によれば、固体電解質電池の薄型化等を
図ることができ、また電池に柔軟性を与えるとと
もに、電池の大面積化も可能になる。さらに電池
組立の際の加工性および生産性にも優れる。
According to the present invention, it is possible to reduce the thickness of a solid electrolyte battery, provide flexibility to the battery, and increase the area of the battery. Furthermore, it has excellent workability and productivity during battery assembly.

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

第1図は、本発明の実施例1に係る固体電解質
電池の断面図、第2図は、本発明の実施例2に係
る固体電解質電池の断面図である。 1……電解質シート、2……正極シート、2a
……正極シート1、2b……正極シート2、2c
……正極シート3、3……負極シート、3a……
負極シート1、3b……負極シート2、3c……
負極シート3,4および5……引き出し電極、6
……封止材。
FIG. 1 is a cross-sectional view of a solid electrolyte battery according to Example 1 of the present invention, and FIG. 2 is a cross-sectional view of a solid electrolyte battery according to Example 2 of the present invention. 1... Electrolyte sheet, 2... Positive electrode sheet, 2a
...Positive electrode sheets 1, 2b...Positive electrode sheets 2, 2c
...Positive electrode sheet 3, 3...Negative electrode sheet, 3a...
Negative electrode sheets 1, 3b... Negative electrode sheets 2, 3c...
Negative electrode sheets 3, 4 and 5... Extraction electrode, 6
... Sealing material.

Claims (1)

【特許請求の範囲】 1 イオン伝導性の無機質固体電解質粉を絶縁性
高分子弾性体中に55〜95%の体積分率で含有させ
分散せしめた電解質シートを、電極活物質粉と無
機質固体電解質粉との混合物を絶縁性高分子弾性
体中に75〜95%の体積分率で含有させ分散せしめ
た負の電極シートと正の電極シートとの間に積層
し、該電極シートに引き出し電極を積層してなる
ことを特徴とする固体電解質電池。 2 電極シートが、電極活物質粉と無機質固体電
解質粉との混合比を段階的に変化せしめた複数の
シートが混合比の順に積層されたものであり、電
極シートの無機質固体電解質粉の混合割合の大き
い面が電解質シートと接するようにしたことを特
徴とする特許請求の範囲第1項記載の固体電解質
電池。
[Scope of Claims] 1. An electrolyte sheet containing and dispersing ion-conducting inorganic solid electrolyte powder in an insulating polymeric elastomer at a volume fraction of 55 to 95%, an electrode active material powder and an inorganic solid electrolyte. A mixture with powder is contained and dispersed in an insulating polymer elastomer at a volume fraction of 75 to 95% and is laminated between a negative electrode sheet and a positive electrode sheet, and an extraction electrode is attached to the electrode sheet. A solid electrolyte battery characterized by being laminated. 2. The electrode sheet is a stack of multiple sheets in which the mixing ratio of the electrode active material powder and the inorganic solid electrolyte powder is changed in stages, and the mixing ratio of the inorganic solid electrolyte powder in the electrode sheet is stacked in the order of the mixing ratio. 2. The solid electrolyte battery according to claim 1, wherein the large surface of the solid electrolyte battery is in contact with the electrolyte sheet.
JP62073728A 1987-03-27 1987-03-27 solid electrolyte battery Granted JPS63239775A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP62073728A JPS63239775A (en) 1987-03-27 1987-03-27 solid electrolyte battery
US07/172,166 US4810599A (en) 1987-03-27 1988-03-23 Structure suitable for solid electrochemical elements
DE3852412T DE3852412T2 (en) 1987-03-27 1988-03-25 Structure, suitable for use in solid electrochemical elements.
EP88104873A EP0284104B1 (en) 1987-03-27 1988-03-25 Structure suitable for solid electrochemical elements
KR1019880003331A KR970004137B1 (en) 1987-03-27 1988-03-26 Structures Suitable as Solid Electrochemical Devices

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62073728A JPS63239775A (en) 1987-03-27 1987-03-27 solid electrolyte battery

Publications (2)

Publication Number Publication Date
JPS63239775A JPS63239775A (en) 1988-10-05
JPH0576138B2 true JPH0576138B2 (en) 1993-10-22

Family

ID=13526581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62073728A Granted JPS63239775A (en) 1987-03-27 1987-03-27 solid electrolyte battery

Country Status (1)

Country Link
JP (1) JPS63239775A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2564193B2 (en) * 1989-12-07 1996-12-18 日本合成ゴム株式会社 Method for manufacturing solid electrolyte battery element
JP5004066B2 (en) * 2001-07-06 2012-08-22 独立行政法人物質・材料研究機構 Multilayer structure and lithium battery using the same
JP5679748B2 (en) * 2010-09-21 2015-03-04 日立造船株式会社 Manufacturing method of all solid state battery
JP5413355B2 (en) * 2010-11-08 2014-02-12 トヨタ自動車株式会社 All solid battery

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Publication number Priority date Publication date Assignee Title
JPS5795083A (en) * 1980-12-05 1982-06-12 Hitachi Maxell Ltd Manufacture of solid electrolyte cell
DE3200757C1 (en) * 1982-01-13 1983-07-21 Fa. Carl Freudenberg, 6940 Weinheim Flexible electrolytic cell

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