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
JP3581774B2 - Aprotic electrolyte thin film and method for producing the same - Google Patents
[go: Go Back, main page]

JP3581774B2 - Aprotic electrolyte thin film and method for producing the same - Google Patents

Aprotic electrolyte thin film and method for producing the same Download PDF

Info

Publication number
JP3581774B2
JP3581774B2 JP10667997A JP10667997A JP3581774B2 JP 3581774 B2 JP3581774 B2 JP 3581774B2 JP 10667997 A JP10667997 A JP 10667997A JP 10667997 A JP10667997 A JP 10667997A JP 3581774 B2 JP3581774 B2 JP 3581774B2
Authority
JP
Japan
Prior art keywords
organopolysiloxane
thin film
aprotic electrolyte
gel
aprotic
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 - Fee Related
Application number
JP10667997A
Other languages
Japanese (ja)
Other versions
JPH10283837A (en
Inventor
公一 河野
耕太郎 滝田
教充 開米
Original Assignee
東燃化学株式会社
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 東燃化学株式会社 filed Critical 東燃化学株式会社
Priority to JP10667997A priority Critical patent/JP3581774B2/en
Publication of JPH10283837A publication Critical patent/JPH10283837A/en
Application granted granted Critical
Publication of JP3581774B2 publication Critical patent/JP3581774B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Primary Cells (AREA)
  • Fuel Cell (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、非プロトン性電解質薄膜及びその製造方法に関し、特にポリオレフィン微多孔膜に、非プロトン性電解質溶液を固定化した非プロトン性電解質薄膜及びその製造方法に関する。
【0002】
【従来の技術】
電解質薄膜は、燃料電池、食塩電解、一次電池、二次電池、促進輸送用分離膜、エレクトロクロミックデバイス、センサーなど低膜抵抗で、かつ優れた機械的強度の要求される分野に広く利用できる。なかでも、リチウム系二次電池などの高分子固体電解質として利用できる。
高分子固体電解質系のリチウム二次電池は、リチウム金属のデンドライトの生成を阻止して電池の短絡損傷や発火問題を解決し、溶液系の二次電池に比べ液洩れがなく、特に薄膜化、大面積化を可能にするということで、開発が望まれてきている。
【0003】
LiClOなどのリチウム塩をポリエチレンオキシドやポリプロピレンオキシドなどのポリエーテル、ポリエステル、ポリイミド、ポリエーテル誘導体に溶解させた高分子電解質が開発されているが、イオン導電率10−5〜10−3Scm−1は室温より十分高温でないと発揮されない。
また、実効抵抗を下げるためには薄膜化の例として、50μm以下の固体高分子多孔薄膜の0.1μm以下の微細な空孔中に毛管凝縮を利用して液体状イオン導電体を固定化する方法(特開平1−158051号)があるが、動作温度の問題は根本的には解決されていなかった。
【0004】
さらに、ポリマーマトリックスに従来の液体タイプのリチウム電池と同じような塩と溶媒の溶液を含浸させるゲル状ポリマーとして、架橋したポリアルキレンオキシドを電解質に用いる技術(USP4,303,748)、ポリアリレートをゲル化して電解質に用いる技術(USP4,830,939)が提案されている。また、最近では、ポリフッ化ビニリデンとヘキサフルオロプロピレンの共重合体にリチウム塩を溶解したカーボネート系溶液を含浸させたポリマーゲルを電解質に用いる技術(USP5,296,318)が提案され、有望視されているが、高温におけるゲル収縮による電解液の滲みだしの問題があり、溶媒保持性に問題があった。
【0005】
【発明が解決しようとする課題】
本発明は、上記のような問題点を解消し、薄膜化、大面積化などが容易で広い温度範囲で非プロトン性電解質溶媒の保持性に優れ、長期安定性と機械的強度の向上した非プロトン性電解質薄膜及びその製造方法を提供することにある。
【0006】
【課題を解決するための手段】
本発明者らは、前記従来技術の問題点を克服するために鋭意研究した結果、ポリオレフィン微多孔膜に含有されたオルガノポリシロキサンの親和性により、非プロトン性電解液を膜に固定化することによって、上記目的を達成できることを見い出した。
【0007】
すなわち、本発明は、非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンを含有するポリオレフィン微多孔膜に、非プロトン性電解質溶液を固定化した非プロトン性電解質薄膜である。
また、本発明の非プロトン性電解質薄膜の第1の製造方法は、ポリオレフィン微多孔膜に、非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンをコーティングし、これに非プロトン性電解質溶液を含浸させて固定化するものである。
さらに、本発明の非プロトン性電解質薄膜の第2の製造方法は、ポリオレフィン組成物からなるゲル状成形物に非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンを充填して製膜し、これに非プロトン性電解質溶液を含浸させて固定化するものである。
【0008】
【発明の実施の形態】
本発明の非プロトン性電解質薄膜は、非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンを含有するポリオレフィン微多孔膜に、非プロトン性電解質溶液を固定化することにより構成される。以下にその詳細を説明する。
【0009】
1.原料
a.ポリオレフィン
ポリオレフィンとしては、ポリエチレン、ポリプロピレン、エチレン−プロピレン共重合体、ポリブテン−1、ポリ4−メチルペンテン−1などが挙げられる。これらの中ではポリエチレンが好ましい。このポリエチレンとしては、超高分子量ポリエチレン、高密度ポリエチレン、中低密度ポリエチレンからなるものを用いることができるが、強度、安全性、製膜性などの観点から超高分子量ポリエチレンまたはその成分を含むものを用いることが好ましい。
また、該ポリオレフィンは、重量平均分子量が5×10以上、好ましくは1×10〜1×10の超高分子量成分を1重量%以上含有し、分子量分布(重量平均分子量/数平均分子量)が10〜300であるのが好ましい。超高分子量ポリオレフィン成分の含有量が1重量%未満では、膜の延伸性の向上に寄与するところが不十分である。一方、上限は特に限定的ではない。また、分子量分布が300を超えると、低分子量成分による破断が起こり薄膜全体の強度が低下するため好ましくない。
【0010】
b.オルガノポリシロキサン
本発明で用いるオルガノポリシロキサンは、1個のケイ素当たり少なくとも1個以上のケイ素−炭素結合を有し、ケイ素−酸素結合(→Si−O−Si←)を繰り返し単位とする高分子化合物である。例えばシリコーンオイル、シリコーン製ゴムとして市販されている重合度が10以上、好ましくは10〜10000のものが利用できる。重合度が10未満では揮発散逸が無視できなくなり好ましくない。一方、重合度が100を大きく超えると高粘度となり、ゲル状成形物へ均一に充填することが困難となるので、揮発性溶剤で希釈することが好ましい。
【0011】
オルガノポリシロキサンの具体例としては、有機基がメチル基であるポリジメチルシロキサンを基本として、ポリシロキサン鎖の末端又は内部に水素、ビニル基、ヒドロキシル基、アミノ基、カルボキシル基、エポキシ基、メタクリロキシ基、メルカプト基、長鎖アルキル基、フェニル基、塩素又はフッ素などが結合した変性ポリシロキサン、更に主鎖に非ポリシロキサン部分を持つもの、例えばアルキレンオキシド変性ポリシロキサン、シリコーン変性共重合体、アルコキシシラン変性重合体などが挙げられる。ポリメチルビニルシロキサン、ポリメチルフェニルビニルシロキサン、ポリメチルフルオロビニルシロキサンあるいは末端が水酸基封鎖されたポリジメチルシロキサンなどポリシロキサン鎖の内部又は末端にビニル基あるいは水酸基などを結合した変性ポリシロキサンも用いることができるが、−(CHCHO)−Rのようなエーテル系基を側鎖に持つ変性ポリシロキサンあるいは−〔(CHCOO(CH〕−Rのようなエステル系基を持つ変性ポリシロキサンは、非プロトン性電解質溶液との親和性だけでなく、リチウムイオンと一種の錯体を形成しイオン伝導促進効果が期待される。
【0012】
重合度の高いオルガノポリシロキサンを希釈する際の揮発性溶剤としては、ペンタン、ヘキサン、ヘプタン、トルエンなどの炭化水素、塩化メチレン、四塩化炭素などの塩素化炭化水素、三塩化三フッ化エタンなどのフッ化炭化水素、ジエチルエーテル、ジオキサンなどのエーテル類、その他、メタノール、エタノールなどのアルコール類が挙げられる。
なお、上記のオルガノポリシロキサンまたはその希釈溶液には、必要に応じてオルガノポリシロキサンの架橋剤、例えば有機過酸化物、3個以上の官能基を有する有機ケイ素化合物、アルキルオルソシリケート、金属系触媒あるいは合成シリカなどの補強材、その他の添加剤を少量調合してもよい。
【0013】
c.電解質溶液
非プロトン性電解質溶液の電解質としては、アルカリ金属塩、アルカリ土類金属塩が用いられ、例えばLiF、NaI、LiI、LiClO、LiAsF、LiPF、LiBF、LiCFSO、NaSCN等が挙げられる。
また、非プロトン性電解質溶液の電解質を溶解する非プロトン性溶媒としては、アルカリ金属に対して安定な溶媒で、具体的には、プロピレンカーボネート、エチレンカーボネート、γ−ブチロラクトン、ジメトキシエタン、アセトニトリル、フォルムアミド、テトラヒドロフラン、ジエチルエーテル等の非プロトン性の高誘電率溶媒が単独または2種類以上の組み合わせで使用される。
【0014】
2.製法
本発明の非プロトン性電解質薄膜の製法は、A.ポリオレフィン微多孔膜にオルガノポリシロキサンをコーティングし、電解質溶液を固定化する方法、B.ポリオレフィン組成物からなるゲル状成形物にオルガノポリシロキサンを充填して製膜し、電解質溶液を固定化する方法、の2通りの製法がある。
【0015】
A.ポリオレフィン微多孔膜にオルガノポリシロキサンをコーティングし、電解質溶液を固定化する方法
A−a.微多孔膜の製法
ポリオレフィン微多孔膜の製造は、特開昭60−242035号や特開平3−64334号に記載の方法で行えばよい。例えば次のようにして行うことができる。まず、ポリオレフィン組成物を溶媒に加熱溶解することにより溶液を調整する。この溶媒としてはポリオレフィン組成物を充分に溶解できるものであれば特に限定されず、特開昭60−242035号などに記載のものと同じでよいが、デカリン、キシレンなどの易揮発性の溶媒も用いることができる。加熱溶解は、ポリオレフィン組成物が溶媒中で完全に溶解する温度で撹拌しながら行う。その温度は使用する重合体及び溶媒により異なるが、140〜250℃の範囲が好ましい。また、ポリオレフィン組成物溶液の濃度は、10〜50重量%、好ましくは10〜40重量%である。
次に、ポリオレフィン組成物の加熱溶液をダイから押し出して成形する。ダイは、通常長方形の口金形状をしたシートダイが用いられるが、2重円筒状の中空糸ダイ、インフレーションダイなども用いることができる。シートダイを用いた場合のダイギャップは通常0.1〜5mmであり、押出し成形時には140〜250℃に加熱される。この際の押出し速度は、通常20〜30cm/分乃至5〜10m/分である。
【0016】
このようにしてダイから押し出された溶液は、冷却することによりゲル状物に成形される。冷却速度は少なくともゲル化温度以下までは50℃/分以上の速度で行うのが好ましい。
次に、このゲル状成形物を延伸する。延伸は、ゲル状成形物を加熱し、通常のテンター法、ロール法、インフレーション法、圧延法もしくはこれらの方法の組合せによって所定の倍率で行う。2軸延伸が好ましく、縦横同時延伸又は逐次延伸のいずれもよいが、特に同時2軸延伸が好ましい。延伸温度は、ポリオレフィン組成物の内、ポリエチレンの融点+10℃以下、好ましくは結晶分散温度から結晶融点未満の範囲である。例えば、90〜140℃、より好ましくは、100〜130℃の範囲である。
さらに、この延伸膜中に含まれる溶媒を塩化メチレンのような揮発性溶剤で抽出除去し、次いで乾燥、熱セットする。
なお、ポリオレフィン微多孔膜には、必要に応じて、酸化防止剤、紫外線吸収剤、滑剤、アンチブロッキング剤、顔料、染料、無機充填剤などの各種添加剤を、本発明の目的を損なわない範囲で添加することができる。
【0017】
上記のポリオレフィン微多孔膜は、1〜1000μm、好ましくは5〜500μmの膜厚を有する。厚さが1μm未満では、機械的強度及び取扱の観点から実用に供することが難しい。一方、1000μmを超える場合には、実効抵抗が大きくなり、非プロトン性電解質薄膜としての体積効率も不利となる。
また、膜の空孔率は、限定的ではないが、30〜95%、より好ましくは50〜90%の範囲のものである。空孔率が30%未満では、非プロトン性電解質溶液の固定化が不十分になる場合があり、一方、空孔率が95%を超えると、膜の機械的強度が小さくなり実用性に劣る。
【0018】
A−b.オルガノポリシロキサンのコーティング方法
オルガノポリシロキサンのコーティング方法としては、上記のポリオレフィン微多孔膜に対して非溶媒である有機溶剤に溶解したオルガノポリシロキサンの溶液をポリオレフィン微多孔膜へスプレー、塗布あるいは該膜を液中に浸漬、その他のコーティング操作が挙げられる。有機溶剤を蒸発固化させた膜はさらに架橋を行うことがより好ましい。コーティングの厚さは、複合膜として1〜1000μmとすることが好ましい。
【0019】
A−c.電解質溶液の固定化方法
オルガノポリシロキサンを含有するポリオレフィン微多孔膜に非プロトン性電解質溶液を固定化し非プロトン性電解質薄膜とする方法としては、含浸、塗布またはスプレーなどを単独あるいは組み合わせて使用することができる。また、電解質溶液を固定化するのは、電池に組み込む前でもよいし、電池組立途中工程でもよいし、電池組立最終工程でもよい。中でも、電池組立時の取扱性、皺などの混入防止、正負極板表面との密着性などの観点と、従来の電池組立工程をそのまま適用できることから、電池組立途中工程あるいは電池組立最終工程で電解質溶液を固定化する方法が好ましい。
なお、電解質溶液含有率は、オルガノポリシロキサンを含有するポリオレフィン微多孔膜の70〜350重量%、好ましくは80〜250重量%である。保持率が70重量%未満では、電解質溶液との界面が少なくなり、電池やコンデンサー及びエレクトロクロミック素子としての応用が実用性の面から制約される。一方、350重量%を超えると、膜の機械的強度が不十分となる。
【0020】
B.ポリオレフィン組成物から成るゲル状成形物にオルガノポリシロキサンを充填して製膜し、電解質溶液を固定化する方法
B−a.ゲル状成形物の作成
ポリオレフィン組成物から成るゲル状シートは、A−aに記載の微多孔膜の製法において延伸工程前のゲル状シートと同様にして作成される。即ち、超高分子量ポリオレフィンを溶媒に加熱溶解し、この溶液をシート状に成形し、冷却することによりゲル状シートを得ることができる。
【0021】
B−b.オルガノポリシロキサンの充填と製膜
オルガノポリシロキサンを充填するため、まず前記のゲル状シート中の溶媒を除去する。除去方法としては、ゲル状シートの加熱による溶媒の蒸発除去、圧縮による除去、揮発性の溶剤による溶媒の抽出除去、凍結乾燥によりゲル状シートの網状組織を保ったままでの溶媒の除去などが挙げられるが、ゲル状シートの構造を著しく変化させることなく溶媒を除去するためには、揮発性溶剤による抽出除去が好ましい。また、ゲル状シート中の溶媒は1重量%以下まで除去することが好ましい。
【0022】
オルガノポリシロキサンの充填は、脱溶媒処理を行ったゲル状シートを、脱溶媒処理の揮発性溶剤の存在下又は不存在下においてオルガノポリシロキサン液もしくはその希釈溶液中に浸漬またはそれをコーティングすることによって行われる。また、脱溶媒処理を施していない未処理のゲル状シートの場合であっても、オルガノポリシロキサン液もしくはその希釈溶液を圧入することによって充填することができる。しかし、脱溶媒処理後の揮発性溶媒存在下でゲル状シートを浸漬する方が容易に充填できるため、より好ましい。
【0023】
オルガノポリシロキサン希釈溶液の希釈濃度は、ゲル状シート中に充填するオルガノポリシロキサンの量によって異なるが、少なくとも0.05重量%以上が好ましく、特に0.5重量%以上が好ましい。濃度が0.05重量%未満ではゲル状シート中に充填されるオルガノポリシロキサンが不足し、延伸時にピンホールが生じやすくなる。また、溶液粘度は、ゲル状シート全体にわたって均一に充填するために、25℃において500cSt未満が好ましく、特に100cSt未満が好ましい。
ゲル状シートへのオルガノポリシロキサンの充填量は、5〜90重量%が好ましく、特に10〜80重量%が好ましい。
次に、得られたオルガノポリシロキサン含有ゲル状シートを延伸する。延伸方法はA−aに記載のゲル状成形物の延伸工程と同様に行うことができる。
【0024】
B−c.電解質溶液の固定化方法
電解質溶液の固定化方法は、A−cに記載した方法と同様にして行うことができる。
【0025】
【実施例】
本発明を以下の具体的な実施例によりさらに詳細に説明するが、本発明は実施例に特に限定されるものではない。なお、実施例における試験方法は次の通りである。
(1)膜厚:断面を走査型電子顕微鏡により測定。
(2)空孔率:重量法により測定。
(3)引張り破断強度:ASTM D882に準拠して測定。
(4)平均孔径:オムニソープ360により測定。
【0026】
実施例1
ポリエチレン微多孔膜(重量平均分子量110万、分子量分布20、膜厚25μm、平均孔径0.03μm、空孔率43.5%、引張強度1049kg/cm)にキシレンで15重量%に希釈した2液型室温硬化シリコンゴムコンパウンド〔KE103RTV(商品名)、信越化学社製〕を塗布し、室温にて24時間放置して、硬化したオルガノポリシロキサンの充填量53重量%の複合膜を得た。
【0027】
このオルガノポリシロキサンを充填したポリエチレン微多孔膜10×10mm角に25℃の1モルのLiPFを含むプロピレンカーボネート溶液を少量滴下し、密閉容器の中に1時間放置して、膨潤率(重量増加率)105%の非プロトン性電解質薄膜を得た。
得られた非プロトン性電解質薄膜を直径10mmに打ち抜き、これを白金黒電極に挟み、周波数1kHzの交流で電気抵抗値を測定し、この値と薄膜の厚み及び面積より算出したイオン導電率は5×10−3Scm−1であった。
【0028】
実施例2
超高分子量ポリエチレン(重量平均分子量2×10)3重量部、高密度ポリエチレン(重量平均分子量4×10)14重量部及び流動パラフィン(64cSt/40℃)83重量部をからなる混合物100重量部に、2,6−ジ−t−ブチル−p−クレゾール0.125重量部とテトラキス〔メチレン−3−(3,5−ジ−t−ブチル−4−ヒドロキシフェニル)プロピオネート〕メタン0.25重量部を酸化防止剤として加え、2軸押出機で加熱混練した。これを長方形の口金を有するダイから押し出し、30℃に温調したチルロールで引き取り2mm厚のシートとした。このシートを多量の塩化メチレン中に60分間浸漬し、次いでこのシートを乾燥させること無く直ちに、メチルビニルシリコーンオイル(日本ユニカー社製、商品名:NUCシリコーンガムストックW−9613)20重量%の塩化メチレン溶液中に移行し60分間浸漬した後、四方を固定した状態で塩化メチレンを乾燥除去してメチルビニルシリコーンオイル充填量49重量%のシートを得た。
【0029】
このメチルビニルシリコーンオイル充填シートをバッチ式2軸延伸機を用いて125℃で5×5倍に同時2軸延伸した。得られた膜の赤外線吸収スペクトルを測定したところ、ビニル基は認められず、また塩化メチレン抽出によるメチルビニルシリコーンオイルの溶出は認められなかった。
このオルガノポリシロキサンを充填したポリエチレン膜を25℃の1モルのLiPFを含むプロピレンカーボネート溶液に1時間浸漬し、膜厚22μm、膨潤率(重量増加率)126%の非プロトン電解質薄膜を得た。
得られた非プロトン電解質薄膜を直径10mmに打ち抜き、これを白金黒電極に挟み、周波数1kHzの交流で電気抵抗値を測定し、この値と薄膜の厚み及び面積より算出したイオン導電率は7×10−3Scm−1であった。
【0030】
実施例3
実施例2において、メチルビニルシリコーンオイルの代わりにジメチルシリコンオイル(日本ユニカー社製、商品名:NUCシリコーンオイルL−45)を用いて充填量45重量%のシートを得、実施例2と同様に延伸製膜し、Co−60線源のγ線を5Mrad照射してオルガノポリシロキサンを充填したポリエチレン膜を得た。得られた膜の塩化メチレン抽出によるジメチルシリコンオイルの溶出は認められなかった。
このオルガノポリシロキサンを充填したポリエチレン膜10×10mm角を25℃の1モルのLiPFを含むプロピレンカーボネート溶液に1時間浸漬し、膜厚23μm、膨潤率(重量増加率)105%の非プロトン電解質薄膜を得た。得られた非プロトン電解質薄膜を直径10mmに打ち抜き、これを白金黒電極に挟み、周波数1kHzの交流で電気抵抗値を測定し、この値と薄膜の厚み及び面積より算出したイオン導電率は6×10−3Scm−1であった。
【0031】
比較例1
実施例1において、オルガノポリシロキサンを充填する前のポリエチレン微多孔膜の10×10mm 角を、25℃の1モルのLiPFを含むプロピレンカーボネート溶液に1時間浸漬し、膨潤率(重量増加率)72.5%の非プロトン性電解質薄膜を得た。
得られた非プロトン性電解質薄膜を直径10mmに打ち抜き、これを白金黒電極で挟み、周波数1kHzの交流で電気抵抗値を測定し、この値と非プロトン性電解質薄膜の厚み及び面積より算出したイオン導電率は3×10−3Scm−1であった。
【0032】
【発明の効果】
本発明の非プロトン性電解質薄膜は、導入したオルガノポリシロキサンの親和性により電解質溶液を固定化し、ポリオレフィンでできた多孔膜基材骨格によりその過度な膨潤を抑えることにより、広い温度範囲で安定的に電解質溶液を保持することができるとともに、電解液溶媒の蒸発速度を極めて低く保つことができる。
またオルガノポリシロキサンの種類を使い分けることにより、使用目的に併せてイオン伝導度を容易に制御することができる。すなわち、イオン導電性を著しく低下させることなく、過充電での安全性を向上することが出来る。
さらにこの非プロトン性電解質薄膜はポリオレフィンでできた骨格により、機械強度が優れており、従来の電池製造工程をほとんど変更することなく適用することができる。また、特にポリオレフィンとして超高分子量ポリエチレン成分を用いた場合、非プロトン性電解質薄膜は機械的強度および耐久性に優れ、非プロトン系電解液を用いる一次電池、二次電池、コンデンサー、中でもリチウム一次電池、リチウム二次電池に好適に用いられる。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an aprotic electrolyte thin film and a method for producing the same, and more particularly to an aprotic electrolyte thin film in which an aprotic electrolyte solution is immobilized on a polyolefin microporous membrane and a method for producing the same.
[0002]
[Prior art]
The electrolyte thin film can be widely used in fields requiring low membrane resistance and excellent mechanical strength, such as fuel cells, salt electrolysis, primary batteries, secondary batteries, separators for facilitated transport, electrochromic devices, and sensors. Among them, it can be used as a solid polymer electrolyte such as a lithium secondary battery.
Polymer solid electrolyte type lithium secondary batteries prevent lithium metal dendrite formation and solve battery short-circuit damage and ignition problems.There is no liquid leakage compared to solution type secondary batteries. Development is desired because it enables a large area.
[0003]
A polymer electrolyte in which a lithium salt such as LiClO 4 is dissolved in a polyether such as polyethylene oxide or polypropylene oxide, a polyester, a polyimide, or a polyether derivative has been developed, and the ionic conductivity is 10 −5 to 10 −3 Scm −. 1 is not exhibited unless it is sufficiently higher than room temperature.
In order to reduce the effective resistance, as an example of thinning, a liquid ionic conductor is immobilized by using capillary condensation in fine pores of 0.1 μm or less of a solid polymer porous thin film of 50 μm or less. Although there is a method (Japanese Patent Laid-Open No. 1-158051), the problem of operating temperature has not been fundamentally solved.
[0004]
Furthermore, as a gel polymer in which a polymer matrix is impregnated with a salt and solvent solution similar to that of a conventional liquid type lithium battery, a technique using a cross-linked polyalkylene oxide as an electrolyte (US Pat. No. 4,303,748) and polyarylate are used. A technique (US Pat. No. 4,830,939) for gelling and using as an electrolyte has been proposed. Recently, a technique using a polymer gel obtained by impregnating a carbonate-based solution obtained by dissolving a lithium salt in a copolymer of polyvinylidene fluoride and hexafluoropropylene (US Pat. No. 5,296,318) has been proposed and is promising. However, there is a problem of oozing out of the electrolytic solution due to gel shrinkage at a high temperature, and there is a problem in solvent retention.
[0005]
[Problems to be solved by the invention]
The present invention solves the above-mentioned problems, facilitates thinning, large area, etc., and has excellent aprotic electrolyte solvent retention over a wide temperature range, and has improved long-term stability and mechanical strength. An object of the present invention is to provide a protic electrolyte thin film and a method for producing the same.
[0006]
[Means for Solving the Problems]
The present inventors have conducted intensive studies to overcome the problems of the prior art, and found that the aprotic electrolyte solution was immobilized on the membrane due to the affinity of the organopolysiloxane contained in the polyolefin microporous membrane. It has been found that the above object can be achieved by the above.
[0007]
That is, the present invention is an aprotic electrolyte thin film in which an aprotic electrolyte solution is immobilized on a polyolefin microporous film containing an organopolysiloxane having an affinity for the aprotic electrolyte solution.
In the first method for producing an aprotic electrolyte thin film of the present invention, a polyolefin microporous membrane is coated with an organopolysiloxane having an affinity for the aprotic electrolyte solution, and impregnated with the aprotic electrolyte solution. And immobilize it.
Further, in the second method for producing an aprotic electrolyte thin film of the present invention, a gel-like molded article comprising a polyolefin composition is filled with an organopolysiloxane having an affinity for an aprotic electrolyte solution to form a film. Is impregnated with an aprotic electrolyte solution to be immobilized.
[0008]
BEST MODE FOR CARRYING OUT THE INVENTION
The aprotic electrolyte thin film of the present invention is constituted by immobilizing an aprotic electrolyte solution on a microporous polyolefin membrane containing an organopolysiloxane having an affinity for the aprotic electrolyte solution. The details will be described below.
[0009]
1. Raw material a. Polyolefin Examples of the polyolefin include polyethylene, polypropylene, ethylene-propylene copolymer, polybutene-1 and poly-4-methylpentene-1. Of these, polyethylene is preferred. As this polyethylene, those composed of ultra-high-molecular-weight polyethylene, high-density polyethylene, and medium-low-density polyethylene can be used, but those containing ultra-high-molecular-weight polyethylene or components thereof from the viewpoint of strength, safety, film-forming properties, etc. It is preferable to use
Further, the polyolefin contains an ultrahigh molecular weight component having a weight average molecular weight of 5 × 10 5 or more, preferably 1 × 10 6 to 1 × 10 7 , at least 1% by weight, and has a molecular weight distribution (weight average molecular weight / number average molecular weight). ) Is preferably from 10 to 300. When the content of the ultrahigh molecular weight polyolefin component is less than 1% by weight, the portion which contributes to the improvement of the stretchability of the film is insufficient. On the other hand, the upper limit is not particularly limited. On the other hand, if the molecular weight distribution exceeds 300, breakage due to low molecular weight components occurs, and the strength of the entire thin film decreases, which is not preferable.
[0010]
b. Organopolysiloxane The organopolysiloxane used in the present invention is a polymer having at least one silicon-carbon bond per silicon and having a silicon-oxygen bond (→ Si—O—Si ←) as a repeating unit. Compound. For example, commercially available silicone oils and silicone rubbers having a polymerization degree of 10 or more, preferably 10 to 10000 can be used. If the degree of polymerization is less than 10, volatile dissipation is not negligible and is not preferred. On the other hand, if the degree of polymerization greatly exceeds 100, the viscosity becomes high and it becomes difficult to uniformly fill the gel-like molded product. Therefore, dilution with a volatile solvent is preferred.
[0011]
Specific examples of the organopolysiloxane include polydimethylsiloxane in which an organic group is a methyl group, and hydrogen, a vinyl group, a hydroxyl group, an amino group, a carboxyl group, an epoxy group, and a methacryloxy group at the end or inside of the polysiloxane chain. , A modified polysiloxane having a mercapto group, a long-chain alkyl group, a phenyl group, chlorine or fluorine bonded thereto, and further having a non-polysiloxane portion in the main chain, for example, an alkylene oxide-modified polysiloxane, a silicone-modified copolymer, an alkoxysilane Modified polymers and the like can be mentioned. Polymethylvinylsiloxane, polymethylphenylvinylsiloxane, polymethylfluorovinylsiloxane, or polydimethylsiloxane with a hydroxyl-terminated end, such as a modified polysiloxane having a vinyl or hydroxyl group bonded to the inside or end of the polysiloxane chain, may also be used. it is, - (CH 2 CH 2 O ) n modified polysiloxane or with an ether-based group in the side chain, such as -R - [(CH 2) m COO (CH 2) n ] ester such as -R The modified polysiloxane having a group is expected to form not only an affinity with an aprotic electrolyte solution but also a kind of complex with lithium ions to promote ionic conduction.
[0012]
Volatile solvents for diluting organopolysiloxanes with high degrees of polymerization include hydrocarbons such as pentane, hexane, heptane, and toluene, chlorinated hydrocarbons such as methylene chloride and carbon tetrachloride, and ethane trifluoride ethane. And ethers such as diethyl ether and dioxane, and alcohols such as methanol and ethanol.
The above-mentioned organopolysiloxane or its diluted solution may contain, if necessary, a crosslinking agent for the organopolysiloxane, for example, an organic peroxide, an organosilicon compound having three or more functional groups, an alkyl orthosilicate, a metal catalyst. Alternatively, a small amount of a reinforcing material such as synthetic silica or other additives may be blended.
[0013]
c. As the electrolyte of the electrolytic solution aprotic electrolytic solution, alkali metal salts, alkaline earth metal salts are used, for example LiF, NaI, LiI, LiClO 4 , LiAsF 6, LiPF 6, LiBF 4, LiCF 3 SO 3, NaSCN And the like.
Further, as the aprotic solvent for dissolving the electrolyte of the aprotic electrolyte solution, a solvent stable to an alkali metal, specifically, propylene carbonate, ethylene carbonate, γ-butyrolactone, dimethoxyethane, acetonitrile, form An aprotic high dielectric constant solvent such as amide, tetrahydrofuran, diethyl ether or the like is used alone or in combination of two or more.
[0014]
2. Production Method The method for producing the aprotic electrolyte thin film of the present invention is described in A. B. a method of coating an organopolysiloxane on a polyolefin microporous membrane and immobilizing an electrolyte solution; There are two production methods: a method in which a gel-like molded product made of a polyolefin composition is filled with an organopolysiloxane to form a film, and an electrolyte solution is fixed.
[0015]
A. Method of coating organopolysiloxane on microporous polyolefin membrane and fixing electrolyte solution Aa. Production of Microporous Membrane A microporous polyolefin membrane may be produced by the method described in JP-A-60-242035 or JP-A-3-64334. For example, it can be performed as follows. First, a solution is prepared by heating and dissolving the polyolefin composition in a solvent. The solvent is not particularly limited as long as it can sufficiently dissolve the polyolefin composition, and may be the same as that described in JP-A-60-242035, but may also be a volatile solvent such as decalin or xylene. Can be used. The heat dissolution is performed while stirring at a temperature at which the polyolefin composition is completely dissolved in the solvent. The temperature varies depending on the polymer and solvent used, but is preferably in the range of 140 to 250 ° C. The concentration of the polyolefin composition solution is 10 to 50% by weight, preferably 10 to 40% by weight.
Next, the heated solution of the polyolefin composition is extruded from a die and molded. As the die, a sheet die having a rectangular base shape is usually used, but a double-cylindrical hollow fiber die, an inflation die and the like can also be used. The die gap when a sheet die is used is usually 0.1 to 5 mm, and is heated to 140 to 250 ° C during extrusion molding. The extrusion speed at this time is usually 20 to 30 cm / min to 5 to 10 m / min.
[0016]
The solution extruded from the die in this manner is formed into a gel by cooling. The cooling rate is preferably at least 50 ° C./min at least up to the gelling temperature.
Next, this gel-like molded product is stretched. The stretching is performed at a predetermined magnification by heating the gel-like molded product and using a usual tenter method, a roll method, an inflation method, a rolling method or a combination of these methods. Biaxial stretching is preferred, and either longitudinal or transverse simultaneous stretching or sequential stretching may be used, but simultaneous biaxial stretching is particularly preferred. The stretching temperature is equal to or lower than the melting point of polyethylene of the polyolefin composition + 10 ° C, preferably in the range from the crystal dispersion temperature to less than the crystal melting point. For example, it is in the range of 90 to 140C, more preferably 100 to 130C.
Further, the solvent contained in the stretched film is extracted and removed with a volatile solvent such as methylene chloride, and then dried and heat-set.
In addition, the polyolefin microporous film may contain various additives such as an antioxidant, an ultraviolet absorber, a lubricant, an antiblocking agent, a pigment, a dye, and an inorganic filler, if necessary, in a range that does not impair the object of the present invention. Can be added.
[0017]
The above-mentioned microporous polyolefin membrane has a thickness of 1 to 1000 µm, preferably 5 to 500 µm. If the thickness is less than 1 μm, it is difficult to practically use from the viewpoint of mechanical strength and handling. On the other hand, if it exceeds 1000 μm, the effective resistance becomes large and the volume efficiency as an aprotic electrolyte thin film becomes disadvantageous.
The porosity of the film is not limited, but is in the range of 30 to 95%, more preferably 50 to 90%. When the porosity is less than 30%, the immobilization of the aprotic electrolyte solution may be insufficient. On the other hand, when the porosity exceeds 95%, the mechanical strength of the membrane becomes small and the practicability is poor. .
[0018]
Ab. Coating method of organopolysiloxane As a coating method of organopolysiloxane, a solution of an organopolysiloxane dissolved in an organic solvent which is a non-solvent for the above-mentioned microporous polyolefin membrane is sprayed, applied or coated on the polyolefin microporous membrane. In a liquid, and other coating operations. More preferably, the film obtained by evaporating and solidifying the organic solvent is further crosslinked. The thickness of the coating is preferably 1 to 1000 μm as a composite film.
[0019]
Ac. Method of fixing electrolyte solution As a method of fixing an aprotic electrolyte solution to a microporous polyolefin membrane containing an organopolysiloxane to form an aprotic electrolyte thin film, impregnation, coating or spraying, etc., may be used alone or in combination. Can be. In addition, the electrolyte solution may be fixed before being incorporated into the battery, during the battery assembly process, or at the final battery assembly process. Among them, from the viewpoints of ease of handling at the time of battery assembly, prevention of wrinkles and the like, adhesion to the positive and negative electrode plate surfaces, and the fact that the conventional battery assembling process can be applied as it is, the electrolyte may be used during the battery assembling process or the battery assembling final process. The method of immobilizing the solution is preferred.
The content of the electrolyte solution is 70 to 350% by weight, preferably 80 to 250% by weight of the microporous polyolefin membrane containing organopolysiloxane. When the retention is less than 70% by weight, the interface with the electrolyte solution is reduced, and the application as a battery, a capacitor, and an electrochromic element is restricted from the viewpoint of practicality. On the other hand, if it exceeds 350% by weight, the mechanical strength of the film becomes insufficient.
[0020]
B. Method of filling organopolysiloxane into a gel-like molded product comprising a polyolefin composition to form a film, and fixing an electrolyte solution Ba-a. Preparation of gel-like molded article A gel-like sheet comprising the polyolefin composition is prepared in the same manner as the gel-like sheet before the stretching step in the method for producing a microporous membrane described in A-a. That is, a gel-like sheet can be obtained by heating and dissolving an ultrahigh molecular weight polyolefin in a solvent, forming the solution into a sheet, and cooling the sheet.
[0021]
B-b. In order to fill the organopolysiloxane and fill the organopolysiloxane, the solvent in the gel sheet is first removed. Examples of the removal method include removal of the solvent by evaporation of the gel-like sheet by heating, removal by compression, extraction and removal of the solvent by a volatile solvent, and removal of the solvent while maintaining the gel-like sheet network by freeze-drying. However, in order to remove the solvent without significantly changing the structure of the gel-like sheet, extraction with a volatile solvent is preferable. Further, it is preferable to remove the solvent in the gel-like sheet to 1% by weight or less.
[0022]
The filling of the organopolysiloxane is performed by dipping or coating the gel-like sheet subjected to the desolvation treatment in an organopolysiloxane liquid or a dilute solution thereof in the presence or absence of a volatile solvent for the desolvation treatment. Done by Further, even in the case of an untreated gel-like sheet that has not been subjected to a solvent removal treatment, it can be filled by press-fitting an organopolysiloxane liquid or a diluted solution thereof. However, it is more preferable to immerse the gel-like sheet in the presence of the volatile solvent after the desolvation treatment, because it can be easily filled.
[0023]
The dilution concentration of the diluted organopolysiloxane solution depends on the amount of the organopolysiloxane filled in the gel sheet, but is preferably at least 0.05% by weight or more, particularly preferably 0.5% by weight or more. If the concentration is less than 0.05% by weight, the amount of the organopolysiloxane filled in the gel-like sheet is insufficient, and pinholes are likely to occur during stretching. Further, the solution viscosity is preferably less than 500 cSt at 25 ° C., particularly preferably less than 100 cSt in order to uniformly fill the entire gel sheet.
The filling amount of the organopolysiloxane in the gel sheet is preferably from 5 to 90% by weight, particularly preferably from 10 to 80% by weight.
Next, the obtained organopolysiloxane-containing gel-like sheet is stretched. The stretching method can be performed in the same manner as the stretching step of the gel-like molded product described in A-a.
[0024]
B-c. Method for Immobilizing Electrolyte Solution The method for immobilizing the electrolyte solution can be performed in the same manner as the method described in Ac.
[0025]
【Example】
The present invention will be described in more detail with reference to the following specific examples, but the present invention is not particularly limited to the examples. In addition, the test method in an Example is as follows.
(1) Film thickness: The cross section was measured by a scanning electron microscope.
(2) Porosity: measured by a gravimetric method.
(3) Tensile breaking strength: Measured according to ASTM D882.
(4) Average pore size: measured by Omnisoap 360.
[0026]
Example 1
A polyethylene microporous membrane (weight average molecular weight 1.1 million, molecular weight distribution 20, film thickness 25 μm, average pore size 0.03 μm, porosity 43.5%, tensile strength 1049 kg / cm 2 ) diluted to 15% by weight with xylene 2 A liquid type room temperature curing silicone rubber compound [KE103RTV (trade name), manufactured by Shin-Etsu Chemical Co., Ltd.] was applied and left at room temperature for 24 hours to obtain a cured organopolysiloxane filled film having a filling amount of 53% by weight.
[0027]
A small amount of a propylene carbonate solution containing 1 mol of LiPF 6 at 25 ° C. was dropped into a 10 × 10 mm square of the polyethylene microporous membrane filled with the organopolysiloxane, and left for 1 hour in a closed container to obtain a swelling ratio (weight increase). (Proportion) of 105% was obtained.
The obtained aprotic electrolyte thin film was punched out to a diameter of 10 mm, this was sandwiched between platinum black electrodes, the electric resistance was measured with an alternating current of 1 kHz, and the ionic conductivity calculated from this value and the thickness and area of the thin film was 5 × 10 −3 Scm −1 .
[0028]
Example 2
100 parts by weight of a mixture composed of 3 parts by weight of ultrahigh molecular weight polyethylene (weight average molecular weight 2 × 10 6 ), 14 parts by weight of high density polyethylene (weight average molecular weight 4 × 10 5 ) and 83 parts by weight of liquid paraffin (64 cSt / 40 ° C.) To 0.1 part by weight of 2,6-di-t-butyl-p-cresol and 0.25 part of tetrakis [methylene-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate] methane A part by weight was added as an antioxidant, and the mixture was heated and kneaded with a twin-screw extruder. This was extruded from a die having a rectangular die and taken up by a chill roll adjusted to a temperature of 30 ° C. to obtain a sheet having a thickness of 2 mm. The sheet was immersed in a large amount of methylene chloride for 60 minutes, and immediately without drying the sheet, 20% by weight of methyl vinyl silicone oil (manufactured by Nippon Unicar, trade name: NUC silicone gum stock W-9613) was used. After being transferred into a methylene solution and immersed for 60 minutes, methylene chloride was dried and removed in a state where the four sides were fixed to obtain a sheet with a methyl vinyl silicone oil filling of 49% by weight.
[0029]
This methyl vinyl silicone oil-filled sheet was simultaneously biaxially stretched 5 × 5 times at 125 ° C. using a batch type biaxial stretching machine. When the infrared absorption spectrum of the obtained film was measured, no vinyl group was recognized, and no elution of methylvinylsilicone oil by methylene chloride extraction was observed.
The polyethylene film filled with this organopolysiloxane was immersed in a propylene carbonate solution containing 1 mol of LiPF 6 at 25 ° C. for 1 hour to obtain an aprotic electrolyte thin film having a thickness of 22 μm and a swelling ratio (weight increase ratio) of 126%. .
The obtained aprotic electrolyte thin film was punched out to a diameter of 10 mm, this was sandwiched between platinum black electrodes, the electric resistance was measured with an alternating current at a frequency of 1 kHz, and the ionic conductivity calculated from this value and the thickness and area of the thin film was 7 × It was 10 −3 Scm −1 .
[0030]
Example 3
In Example 2, a sheet having a filling amount of 45% by weight was obtained using dimethyl silicone oil (trade name: NUC silicone oil L-45, manufactured by Nippon Unicar) instead of methyl vinyl silicone oil. Stretched film was formed and irradiated with 5 Mrad of γ-ray from a Co-60 radiation source to obtain a polyethylene film filled with organopolysiloxane. No dimethyl silicone oil was eluted by methylene chloride extraction of the obtained membrane.
A 10 × 10 mm square polyethylene film filled with this organopolysiloxane is immersed in a propylene carbonate solution containing 1 mol of LiPF 6 at 25 ° C. for 1 hour, and a non-proton electrolyte having a thickness of 23 μm and a swelling ratio (weight increase ratio) of 105% is used. A thin film was obtained. The obtained aprotic electrolyte thin film was punched out to a diameter of 10 mm, this was sandwiched between platinum black electrodes, the electric resistance was measured with an alternating current at a frequency of 1 kHz, and the ionic conductivity calculated from this value and the thickness and area of the thin film was 6 × It was 10 −3 Scm −1 .
[0031]
Comparative Example 1
In Example 1, a 10 × 10 mm square of the microporous polyethylene membrane before being filled with the organopolysiloxane was immersed in a propylene carbonate solution containing 1 mol of LiPF 6 at 25 ° C. for 1 hour, and a swelling rate (weight increase rate) was obtained. A 72.5% aprotic electrolyte thin film was obtained.
The obtained aprotic electrolyte thin film was punched out to a diameter of 10 mm, sandwiched between platinum black electrodes, measured for electrical resistance with an alternating current at a frequency of 1 kHz, and ion-calculated from this value and the thickness and area of the aprotic electrolyte thin film. The conductivity was 3 × 10 −3 Scm −1 .
[0032]
【The invention's effect】
The aprotic electrolyte thin film of the present invention is stable over a wide temperature range by immobilizing the electrolyte solution by the affinity of the introduced organopolysiloxane and suppressing its excessive swelling by the porous membrane base skeleton made of polyolefin. And the evaporation rate of the electrolyte solvent can be kept extremely low.
In addition, the ionic conductivity can be easily controlled according to the purpose of use by properly selecting the type of the organopolysiloxane. That is, safety in overcharging can be improved without significantly lowering ionic conductivity.
Further, the aprotic electrolyte thin film has excellent mechanical strength due to a skeleton made of polyolefin, and can be applied with almost no change in a conventional battery manufacturing process. In particular, when an ultra-high molecular weight polyethylene component is used as the polyolefin, the aprotic electrolyte thin film has excellent mechanical strength and durability, and a primary battery, a secondary battery, a capacitor using an aprotic electrolyte, particularly a lithium primary battery. And a lithium secondary battery.

Claims (6)

非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンを含有するポリオレフィン微多孔膜に、非プロトン性電解質溶液を固定化した非プロトン性電解質薄膜。An aprotic electrolyte thin film comprising an aprotic electrolyte solution immobilized on a polyolefin microporous membrane containing an organopolysiloxane having an affinity for an aprotic electrolyte solution. ポリオレフィン微多孔膜に、非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンをコーティングし、これに非プロトン性電解質溶液を含浸させて固定化する非プロトン性電解質薄膜の製造方法。A method for producing an aprotic electrolyte thin film comprising coating a polyolefin microporous membrane with an organopolysiloxane having an affinity for an aprotic electrolyte solution, impregnating the coating with an aprotic electrolyte solution, and immobilizing the resultant. ポリオレフィン組成物から成るゲル状成形物に非プロトン性電解質溶液に親和性を有するオルガノポリシロキサンを充填して製膜し、これに非プロトン性電解質溶液を含浸させて固定化する非プロトン性電解質薄膜の製造方法。An aprotic electrolyte thin film in which a gel-like molded product composed of a polyolefin composition is filled with an organopolysiloxane having an affinity for an aprotic electrolyte solution to form a film, which is then impregnated with the aprotic electrolyte solution and immobilized. Manufacturing method. 前記ゲル状成形物が、ポリオレフィンを溶媒に加熱溶解し、この溶液をシート状に成形し、冷却することにより得、オルガノポリシロキサンを充填する前にゲル状シート中の溶媒を除去することを特徴とする請求項3に記載の非プロトン性電解質薄膜の製造方法。The gel-like molded product is obtained by heating and dissolving a polyolefin in a solvent, shaping the solution into a sheet, and cooling it, and removing the solvent in the gel-like sheet before filling with the organopolysiloxane. The method for producing an aprotic electrolyte thin film according to claim 3. オルガノポリシロキサンを充填して得られたオルガノポリシロキサン含有ゲル状シートを延伸することを特徴とする請求項3又は4に記載の非プロトン性電解質薄膜の製造方法。The method for producing an aprotic electrolyte thin film according to claim 3 or 4, wherein the organopolysiloxane-containing gel-like sheet obtained by filling the organopolysiloxane is stretched. 請求項1に記載の非プロトン性電解質薄膜を用いたリチウム電池。A lithium battery using the aprotic electrolyte thin film according to claim 1.
JP10667997A 1997-04-09 1997-04-09 Aprotic electrolyte thin film and method for producing the same Expired - Fee Related JP3581774B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10667997A JP3581774B2 (en) 1997-04-09 1997-04-09 Aprotic electrolyte thin film and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10667997A JP3581774B2 (en) 1997-04-09 1997-04-09 Aprotic electrolyte thin film and method for producing the same

Publications (2)

Publication Number Publication Date
JPH10283837A JPH10283837A (en) 1998-10-23
JP3581774B2 true JP3581774B2 (en) 2004-10-27

Family

ID=14439761

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10667997A Expired - Fee Related JP3581774B2 (en) 1997-04-09 1997-04-09 Aprotic electrolyte thin film and method for producing the same

Country Status (1)

Country Link
JP (1) JP3581774B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105448537B (en) * 2015-12-09 2017-10-27 华东理工大学 Stretchable gel of modified polyolefine elastomer and application thereof
US20250065276A1 (en) * 2021-10-22 2025-02-27 Nissan Chemical Corporation Membrane formation composition, and gas permeation membrane

Also Published As

Publication number Publication date
JPH10283837A (en) 1998-10-23

Similar Documents

Publication Publication Date Title
US10249863B2 (en) Microporous material and a method of making same
KR101174995B1 (en) Microporous membranes and methods for making and using such membranes
JP5453272B2 (en) Microporous membranes and methods of making and using such membranes
US8027147B2 (en) Ultracapacitor and method of manufacturing the same
JP2011500881A5 (en)
WO2010008003A1 (en) Separator for electricity storage device
JP2013166804A (en) Polyolefin microporous membrane, separator for battery and battery
JP2002256093A (en) Porous film, its production method and its use
EP0760383B1 (en) Ion-conductive film and precursor film therefor
KR102107794B1 (en) A composite membrane and a method for manufacturing thereof
JP3581774B2 (en) Aprotic electrolyte thin film and method for producing the same
CN116724371A (en) Polyolefin microporous membranes, battery separators and secondary batteries
JP3586536B2 (en) Immobilized liquid film conductor
JP3919346B2 (en) Polymer solid electrolyte thin film and method for producing the same
JP2022048518A (en) Polyolefin microporous film, and coating film and secondary battery including the same
JP2003026847A (en) Porous film
JP4245239B2 (en) Porous film
JP4307065B2 (en) Method for producing polyolefin microporous membrane
JP3927638B2 (en) Aprotic electrolyte thin film and method for producing the same
JP3586535B2 (en) Immobilized liquid film conductor
KR101692412B1 (en) Polyolefin film with improved physical properties and electrochemical device comprising the same as separator substrate
JP3581772B2 (en) Aprotic electrolyte thin film and method for producing the same
JP2025171376A (en) Separator for non-aqueous battery and non-aqueous battery using the same
JP2022036034A (en) Polyolefin microporous film
JPH10269846A (en) Fixed liquid film conductor

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040531

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040706

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040726

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080730

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080730

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090730

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090730

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100730

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110730

Year of fee payment: 7

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110730

Year of fee payment: 7

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110730

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120730

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120730

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130730

Year of fee payment: 9

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130730

Year of fee payment: 9

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees