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JP3533893B2 - Non-aqueous electrolyte secondary battery - Google Patents
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JP3533893B2 - Non-aqueous electrolyte secondary battery - Google Patents

Non-aqueous electrolyte secondary battery

Info

Publication number
JP3533893B2
JP3533893B2 JP20566497A JP20566497A JP3533893B2 JP 3533893 B2 JP3533893 B2 JP 3533893B2 JP 20566497 A JP20566497 A JP 20566497A JP 20566497 A JP20566497 A JP 20566497A JP 3533893 B2 JP3533893 B2 JP 3533893B2
Authority
JP
Japan
Prior art keywords
battery
positive electrode
lithium
aqueous electrolyte
electrolyte secondary
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
JP20566497A
Other languages
Japanese (ja)
Other versions
JPH1154154A (en
Inventor
義幸 尾崎
憲樹 村岡
茂雄 小林
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.)
Panasonic Corp
Panasonic Holdings Corp
Original Assignee
Panasonic Corp
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 Panasonic Corp, Matsushita Electric Industrial Co Ltd filed Critical Panasonic Corp
Priority to JP20566497A priority Critical patent/JP3533893B2/en
Publication of JPH1154154A publication Critical patent/JPH1154154A/en
Application granted granted Critical
Publication of JP3533893B2 publication Critical patent/JP3533893B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

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

  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は非水電解液二次電池
の高温保存特性の改良に関するものである。 【0002】 【従来の技術】近年、電子機器のポータブル化,コード
レス化が急速に進んでおり、これらの駆動用電源を担う
小型,軽量で高エネルギー密度を有する電池への要望が
高まっている。このような観点から非水系二次電池、と
りわけリチウムイオン二次電池は高電圧,高エネルギー
密度を有する電池として、ノートパソコン,携帯電話,
AV機器などを中心にそれまで主流を占めていたアルカ
リ水溶液系のニカド電池あるいはニッケル水素電池に置
き換わる存在に至り、今後も大きな成長が期待されてい
る。 【0003】現在、実用化されているリチウムイオン二
次電池は正極活物質にLiCoO2などのリチウム含有
遷移金属酸化物を、負極にはリチウムを吸蔵したり放出
し得る炭素材料を用いた電池系が市販されている。この
ような電池系においては、充電時に正極からリチウムイ
オンがデインターカレートし、負極である炭素中にイン
ターカレートすることで充電反応が完了する。放電は充
電反応と逆の反応が進行し、炭素負極からデインターカ
レートしたリチウムイオンが正極活物質中に戻ることで
放電反応が完了する。正極活物質がLi1-xCoO
2 (但し0≦x≦1.0とする)の場合、充電時にデイ
ンターカレートし得るリチウムの反応電子数はx=0.
5電子程度であり、正極比容量に換算すると、約130
mAh/gになる。しかしながら、LiCoO2 はフル
充電状態では4.3Vvs.Li/Li+程度と高電位
にあり、且つx=0.5のリチウムがデインターカレー
トされていることから、その結晶構造は非常に不安定な
状態にある。このような充電状態の電池を例えば45℃
〜85℃程度の高温に放置した場合、正極活物質の特性
劣化が起こるのみならず、反応活性であることから電解
液中の有機溶媒を分解しガス発生を伴うことが知られて
いる。 【0004】一般にリチウムイオン二次電池では過充電
時の安全性確保のために、電池内圧が一定の値を越えた
場合、封口板内に設けられた安全機構が作動し外部から
の電流を遮断するといった安全構造を用いる場合が多
い。しかしながら、上述のような電池を高温に放置し、
ガスが多量に発生した場合、安全機構が作動し電池とし
ての機能を失う可能性がある。そこで電池の高温放置に
おける信頼性と過充電時の安全性確保を両立させるため
に、封口板内に設けられた一定の範囲の内圧で作動する
安全機構を厳密に制御することが要求される。一方で高
温放置におけるガス発生量を最小限に抑制する試みがな
されており、正極材料の物性を制御し、反応性を低下さ
せることや耐電圧特性の良好な電解液を用いることが提
案されてきた。 【0005】最近になって、リチウムイオン二次電池の
更なる高容量化に向けてLiCoO2に代わる正極活物
質としてLiNiO2やNi元素の一部を他元素、例え
ばCoまたはAlまたはMnまたはBなどで置換した固
溶体が提案され(例えば特開平6−60887号公報参
照)その開発が進んでいる。LiNiO2 は充電時にデ
インターカレートし得るリチウム量が大きく180mA
h/g〜200mAh/gの比容量が得られることから
その期待が大きいが、充電状態においてはLiCoO2
よりも更に結晶構造が不安定で且つ反応活性であるため
に高温放置時のガス発生を抑制することが更に必要とさ
れる。 【0006】 【発明が解決しようとする課題】前述のように、リチウ
ム含有遷移金属酸化物を正極活物質に用いた非水電解液
二次電池を充電状態で高温放置した場合、電解液の分解
に伴うガス発生によって電池内圧が上昇し、安全機構の
作動によって電流を遮断してしまうという不具合が起こ
る可能性があり、これを回避するために正極活物質の材
料物性を制御し、粉体および電極の比表面積を低減させ
る試みやガス発生の少ない電解液を選択する試みがされ
た。しかしながらこのような対策を施すと、多くの場合
が電池容量の低下、高率充放電特性の低下などをもたら
し、満足のいく電池特性を引き出すことが困難となる。 【0007】そこで、本発明は上記のような問題点を解
決して、電池容量や高率充放電特性などの電池特性を損
なうことなく、電池を高温放置した場合の電池内圧を低
く抑制する非水電解液二次電池を提供することを目的と
する。 【0008】 【課題を解決するための手段】上記の課題を解決するた
めに本発明は、リチウム含有遷移金属酸化物を主体とす
る正極と、リチウムを活物質とする負極と、非水電解液
とを備えた非水電解液二次電池において、電池系内に発
生するガスと反応して炭酸塩を生成し得るSrOを粉末
あるいは成型体など固体の状態で電極および電解液とは
直接接触しないように配置した非水電解液二次電池とし
たものである 【0009】この発明によれば、充電状態の電池が高温
に放置された場合、電解液の分解により発生したガスと
添加した酸化物が反応してガスを少なくすることによっ
て電池内圧の上昇を抑制することが可能となるものであ
る。 【0010】電池特性の低下を引き起こすことなく高温
放置時のガス発生による電池内圧の上昇を防ぐために
は、発生したガスを封口板内の安全機構が作動する前に
吸収することにより電池内圧の上昇を防止することが有
効である。 【0011】そこで、まず発生するガスの組成分析を行
った結果、ガスの成分のほとんどが炭酸ガスであること
を解明した。また、発生源としては正極に起因するガス
量が支配的であることを解明した。更にガス発生量とし
ては例えば電池を85℃に放置した場合、時間に比例し
てガス量は増え数時間から約10時間程度でガス発生量
はほぼ一定となりそれ以上は発生しないことがわかっ
た。そこで本発明では炭酸ガスとゆるやかに反応を起こ
し、電池性能に悪影響を与えない材料を電池および電解
液とは直接接触しないように電池系内に設置することと
したものである。 【0012】その結果、炭酸塩を生成する酸化物として
SrO,CaO,BaO,MgOの群の中の少なくとも
一つの酸化物を添加することで本発明の効果が得られる
ことを見い出したものである。 【0013】特開平7−153496号公報には、正極
中に活物質とBaO,MgO,CaOから選ばれた少な
くとも1種類以上の酸化物を添加,混合することで電池
のサイクル特性を改善することが開示されているが、本
発明はSrO,BaO,MgO,CaOから選ばれた少
なくとも一つの酸化物を正極中に添加,混合するのでは
なく、粉末あるいは成型体など固体の状態で電極および
電解液とは直接接触しないように配置するものであり、
両者の課題が全く異なり、従って酸化物の配置形態も異
なるものである。 【0014】これら酸化物は炭酸ガスとゆるやかに反応
し炭酸塩を生成し電池系内で安定に存在することから、
電池性能の低下を引き起こすことはない。なお、先に述
べた過充電時の安全性確保に関しては、過充電時には電
解液の分解によるガス発生に優先して正極活物質そのも
のの分解による酸素発生が起こり、その反応速度は高温
放置時のガス発生速度に比べ圧倒的に速い。従って、電
池内圧は上昇し安全機構が作動することになるから、過
充電に対する安全性は確保される。 【0015】 【発明の実施の形態】本発明は請求項に記載した形態で
実施できるものであり、請求項1に記載のように、リチ
ウム含有遷移金属酸化物を主体とする正極と、リチウム
を活物質とする負極と、非水電解液とを備えた非水電解
液二次電池において、電池系内に発生する炭酸ガスと反
応して炭酸塩を生成し得るSrOを粉末あるいは成型体
など固体の状態で電極および電解液とは直接接触しない
ように配置することにより、この酸化物が正極,負極,
電解液とは別に電池系内に存在した場合、電池を高温放
置した際に発生する炭酸ガスと反応し、SrCO 3 を生
成する。生成したSrCO3は比較的不活性であり
池系内で安定に存在しその後の電池特性に悪影響を与
えることはない。 【0016】 【0017】 【0018】 【0019】 【0020】 【0021】 【実施例】以下、実施例により本発明を詳しく述べる。 【0022】(実施例1)図1に本実施例,従来例およ
び比較例で用いた円筒形電池の断面切欠斜視図を示す。
図1において、1は負極リード板2を取り付けた負極
板、3は正極リード板4を取り付けた正極板である。負
極板1と正極板3はセパレータ5を介して渦巻き状に捲
回された極板群をその上下に絶縁板6を配置した状態で
負極端子を兼ねる電池ケース7内に収納されている。電
池ケース7の上縁は絶縁パッキング8を介して、案全弁
を設けた正極端子を兼ねた封口板9で密封されている。
封口板9の内部は電池内圧が20℃で10kg/cm2
を越えると正極端子と正極リード板4の導通がなくなり
外部からの電流を遮断するように設計されている。以
下、正極板と負極板の製造方法などについて詳しく説明
する。 【0023】正極活物質にはLiNi0.8Co0.22
用いた。まず、水酸化ニッケルと水酸化コバルトと水酸
化リチウムとをNi:Co:Liの原子比が0.8:
0.2:1.0になるように秤量し、ボールミルで充分
に混合した。そしてこの混合物をアルミナ製のるつぼに
入れ、酸素中において750℃で10時間の熱処理を行
った。そして自然冷却後、粉砕,分級を行い平均粒径約
10μmの正極活物質粉末とした。この活物質100重
量部に人造黒鉛粉末6重量部を加え、この混合物にN−
メチルピロリドン(以下、NMPという)の溶媒に結着
剤としてのポリフッ化ビニリデン(以下、PVDFとい
う)を溶解した溶液を混練してペースト状にした。な
お、加えたPVDFの量は活物質100重量部に対して
4重量部となるように調製した。次いでこのペーストを
アルミニウム箔の両面に塗工し、乾燥後、圧延して厚み
0.14mm,幅37mm,長さ380mmの正極板と
した。なお、正極板の作製に当たっては混練以降一連の
工程は乾燥空気中で行った。 【0024】負極には平均粒径6.0μmのメソフェー
ズ小球体を2800℃で熱処理し黒鉛化したものを用い
た。この黒鉛化メソフェーズ100重量部に結着剤とし
てのスチレン/ブタジエンゴム3重量部を混合し、カル
ボキシメチルセルロース水溶液を加えて混練し、ペース
ト状にした。そしてこのペーストを銅箔の両面に塗工
し、乾燥後、圧延して厚み0.20mm,幅39mm,
長さ420mmの負極板とした。 【0025】そして正極板,負極板にそれぞれリード板
を取り付け、厚み0.025mm,幅45mm,長さ1
000mmのセパレータを介して渦巻き状に捲回し、直
径17.0mm,高さ50mmの電池ケースに収納し
た。 【0026】続いて添加する酸化物であるが、平均粒径
約8μmのSrOを正極板の作製と同様の方法でNMP
の溶媒に結着剤としてのPVDFを溶解した溶液を混練
してペースト状にした。このペーストをアルミニウム箔
の片面に塗工し、乾燥,圧延した後、直径8mmの円形
に打ち抜き封口板の底部にアルミニウム箔面を溶着し
た。酸化物層の厚みはアルミニウム箔の厚みを含めて
0.08mmとした。また、SrOの充填量は正極活物
質であるLiNi0.8Co0.22 1グラムに対して0.
1ミリモルとした。 【0027】電解液にはエチレンカーボネート(以下、
ECという)とジメチルカーボネート(以下、DMCと
いう)とを20:80の体積比で混合した溶媒に電解質
として1モル/リットルのLiPF6 を溶解したものを
注液した。その際、電解液が封口板底部に配置した酸化
物層に接触しないようにした。そして電解液が充分に極
板群に吸収された後、電池を封口し完成電池とし、実施
例1の電池として20セル作製した。 【0028】(従来例)SrO酸化物を電池系内に配置
しないで、それ以外は実施例1と全く同様に電池を作製
し、従来例の電池として20セル作製した。 【0029】(比較例)実施例1と同量のSrO粉末を
封口板の底部に配置するのではなく、予め正極中に混入
した状態で電池系内に添加した。この正極中にSrOを
添加すること以外は実施例1と全く同様にして電池を作
製し、比較例の電池として20セル作製した。 【0030】そしてこれら実施例1,従来例および比較
例の電池の充放電試験を行った。充電は定電流電圧充電
とし、630mAの定電流で4.2Vまで充電し、4.
2V到達後は定電圧充電に変換し2時間で充電が終了す
るようにした。放電は900mAの定電流放電を行い放
電終止電圧を2.5Vとした。このような充放電を20
℃の環境下で5サイクル行い、3サイクル目の容量を初
期容量とした。そして充電状態の電池を85℃の恒温槽
に15時間放置した。その後20℃の環境下に戻し電池
の導通を測定した。その後、導通のある電池については
再び充放電を行い、3サイクル目の容量を放置後の容量
とした。電池内圧が約10kg/cm2を越えると封口
板9内に設けられた安全機構が作動し、正極,負極間の
導通がなくなることから高温放置によって安全機構が作
動した割合を求めた。また、初期容量,放置後の容量の
平均値と共に結果を表1に示した。 【0031】 【表1】 【0032】高温放置後の電池容量については安全機構
が作動しなかった電池について測定した。実施例1の電
池では全セルが高温放置後も導通があり、安全機構が作
動していないことを示している。つまり、高温放置時に
発生したガスを内部に設けたSrOが吸収したことによ
り電池内圧が所定の値以下に収まっているものと考えら
れる。高温放置後の電池容量も938mAhと大きく、
SrOの反応生成物が電池特性に悪影響を与えていない
ことがわかる。一方、従来例の電池では15セルが高温
放置によって電池内圧の上昇と共に安全機構が作動して
おり、電池としての機能を失っている。また、比較例の
電池もほぼ同様の14セルが安全機構が作動する結果と
なった。また、電池容量も幾分小さくなる傾向にあり好
ましくない。以上のことから、本発明の効果を得るため
にはSrOを正極中に添加,混合することでは目的を達
成することができず、電極および電解液とは直接接触し
ないように電池系内に配置することが重要であることが
わかる。 【0033】また、実施例1の電池と同様の電池を別に
10セル作製し1Aの定電流で過充電試験を行った。い
ずれの電池も18分〜20分後に安全機構が作動し、外
部からの電流を遮断した。電池の発火,破裂,白煙など
は見られず、電池表面温度は約50℃であった。つま
り、電池系内にSrOが存在していても過充電時のガス
吸収は起こっていないか、あるいはその速度が遅いこと
が予想され、本発明は過充電時における安全性を損なう
ものではないことがわかる。 【0034】(参考例)実施例1の電池において添加す
る酸化物としてSrOの代わりにBaOを用い、その添
加量を正極活物質1グラムに対して表2に示す割合で添
加した電池を作製し、それぞれ電池A,電池B,電池
C,電池D,電池E,電池Fとした。これらの電池を実
施例1の電池と同様に充放電を行い、充電状態で高温放
置した。その後の電池の導通を測定し結果を表2に示し
た。 【0035】 【表2】 【0036】電池B,電池C,電池D,電池Eではいず
れも安全機構は作動しておらず、本発明の効果が得られ
ている。しかしながら、添加量が0.03ミリモルと少
ない電池Aでは約半数のセルの安全機構が作動してお
り、電池内圧の抑制が不充分であることがわかる。 【0037】一方、添加量が0.25ミリモルと最も多
い電池Fでも一部安全機構が作動した電池が見られた。
これは添加したBaOの体積が大きくなったために電池
内の空隙体積が極端に小さくなり、ガス吸収反応よりも
電池内圧の上昇速度の方が速くなり安全機構が作動して
しまったものと考えられる。これらの結果から、添加す
る酸化物の量としては正極活物質1グラム当たり0.0
4ミリモル〜0.20ミリモルであることが重要である
といえる。 【0038】なお、実施例1および参考例において正極
活物質にLiNi0.8Co0.22を用いたが、LiNi
2を始めNiの一部を他の元素としてAlまたはMn
またはBで置換した固溶体やLiCoO2,LiMn2
4を用いた場合も同様な効果が得られた。本発明はリチ
ウム含有遷移金属酸化物を正極に用いた非水電解液二次
電池に適用可能である。 【0039】また、負極として、メソフェーズ小球体を
黒鉛化したものを用いたが、他の炭素材料、例えば人工
黒鉛やコークス類,炭素繊維類など、また金属酸化物な
どリチウムを吸蔵したり放出し得るもの、リチウム合金
やリチウム金属を用いた場合など、リチウムを活物質と
した非水電解液二次電池に適用できるものである。 【0040】 【0041】また、電解液であるが、本実施例では溶媒
にECとDMCの混合溶媒を用いたが、他の溶媒として
プロピレンカーボネート,ブチレンカーボネートなどの
環状カーボネート類、ジエチルカーボネート,エチルメ
チルカーボネートなどの鎖状カーボネート類、1,2−
ジメトキシエタン,2−メチルテトラヒドロフランなど
のエーテル類など公知のものがいずれも単独あるいは混
合溶媒として使用可能である。溶質についてもLiBF
4 ,LiClO4 などの公知のものが使用可能である。 【0042】 【発明の効果】以上のように本発明によれば、電池特性
を満足し、且つ、電池が充電状態において高温に放置さ
れた場合においても電池内圧の上昇を抑制し電池として
の機能を喪失させないという有利な効果が得られる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in high-temperature storage characteristics of a non-aqueous electrolyte secondary battery. 2. Description of the Related Art In recent years, portable and cordless electronic devices have been rapidly advanced, and there is an increasing demand for small, lightweight, high-energy-density batteries that serve as driving power supplies for these devices. From this point of view, non-aqueous secondary batteries, especially lithium ion secondary batteries, are high-voltage, high-energy density batteries such as notebook computers, mobile phones,
Alkaline aqueous solution-based nickel-cadmium batteries or nickel-metal hydride batteries have been replaced by alkaline aqueous solution-based nickel-cadmium batteries or nickel-metal hydride batteries, mainly for AV equipment, and large growth is expected in the future. At present, a lithium-ion secondary battery that has been put into practical use is a battery system using a lithium-containing transition metal oxide such as LiCoO 2 as a positive electrode active material and a carbon material capable of occluding and releasing lithium as a negative electrode. Is commercially available. In such a battery system, the lithium ion is deintercalated from the positive electrode during charging and intercalated into carbon as the negative electrode, whereby the charging reaction is completed. In the discharge, a reaction reverse to the charge reaction proceeds, and the lithium ion deintercalated from the carbon negative electrode returns to the positive electrode active material, thereby completing the discharge reaction. The positive electrode active material is Li 1-x CoO
2 (where 0 ≦ x ≦ 1.0), the number of reactive electrons of lithium that can be deintercalated during charging is x = 0.
It is about 5 electrons, which translates into about 130
mAh / g. However, LiCoO 2 is 4.3 Vvs. Since lithium having a high potential of about Li / Li + and x = 0.5 is deintercalated, its crystal structure is in a very unstable state. A battery in such a charged state is, for example,
It is known that when left at a high temperature of about 85 ° C., not only does the property of the positive electrode active material deteriorate, but also because it is reactive, it decomposes the organic solvent in the electrolytic solution and generates gas. In general, in order to ensure safety during overcharge in a lithium ion secondary battery, when the internal pressure of the battery exceeds a certain value, a safety mechanism provided in a sealing plate is activated to cut off an external current. Often, a safety structure is used. However, leaving such batteries at high temperatures,
If a large amount of gas is generated, the safety mechanism may be activated and the function as a battery may be lost. Therefore, in order to achieve both reliability when the battery is left at a high temperature and safety during overcharging, it is required to strictly control a safety mechanism provided within the sealing plate and operating at a certain range of internal pressure. On the other hand, attempts have been made to minimize the amount of gas generated during high-temperature storage, and it has been proposed to control the physical properties of the positive electrode material, reduce the reactivity, and use an electrolytic solution having good withstand voltage characteristics. Was. Recently, LiNiO 2 or a part of Ni element has been replaced with another element such as Co or Al or Mn or B as a cathode active material in place of LiCoO 2 in order to further increase the capacity of a lithium ion secondary battery. A solid solution substituted by, for example, has been proposed (for example, see JP-A-6-60887), and its development is in progress. LiNiO 2 has a large amount of lithium that can be deintercalated at the time of charging and is 180 mA.
Although h / g~200mAh / g of the expected since the specific capacity is obtained is large, the state of charge LiCoO 2
Further, since the crystal structure is more unstable and reactive, it is further necessary to suppress the generation of gas when left at high temperature. [0006] As described above, when a non-aqueous electrolyte secondary battery using a lithium-containing transition metal oxide as a positive electrode active material is left at a high temperature in a charged state, decomposition of the electrolyte occurs. The internal pressure of the battery rises due to the gas generation accompanying it, and there is a possibility that the malfunction of interrupting the current by the operation of the safety mechanism may occur.To avoid this, control the material properties of the positive electrode active material, Attempts have been made to reduce the specific surface area of the electrode and to select an electrolyte that produces less gas. However, when such measures are taken, in many cases, the battery capacity is reduced, the high-rate charge / discharge characteristics are reduced, and it is difficult to obtain satisfactory battery characteristics. Therefore, the present invention solves the above-mentioned problems, and does not impair battery characteristics such as battery capacity and high-rate charge / discharge characteristics without lowering battery internal pressure when the battery is left at high temperatures. It is an object to provide a water electrolyte secondary battery. [0008] In order to solve the above-mentioned problems, the present invention provides a positive electrode mainly composed of a lithium-containing transition metal oxide, a negative electrode mainly composed of lithium, and a non-aqueous electrolyte.
In a non-aqueous electrolyte secondary battery provided with: SrO capable of reacting with a gas generated in the battery system to generate a carbonate does not come into direct contact with an electrode and an electrolyte in a solid state such as a powder or a molded body. The non-aqueous electrolyte secondary battery is arranged as described above . According to the present invention, when a charged battery is left at a high temperature, the gas generated by the decomposition of the electrolytic solution reacts with the added oxide to reduce the gas, thereby suppressing an increase in the internal pressure of the battery. It is possible to do. In order to prevent an increase in the internal pressure of the battery due to gas generation when left at a high temperature without causing a decrease in the battery characteristics, the generated gas is absorbed before the safety mechanism in the sealing plate operates to increase the internal pressure of the battery. It is effective to prevent this. Then, as a result of analyzing the composition of the generated gas, it was found that most of the components of the gas were carbon dioxide. In addition, it was clarified that the amount of gas originating from the positive electrode was dominant as the generation source. Further, as for the gas generation amount, for example, when the battery was left at 85 ° C., the gas amount increased in proportion to the time, and the gas generation amount was substantially constant from several hours to about 10 hours, and no more gas was generated. Therefore, in the present invention, a material that reacts slowly with carbon dioxide and does not adversely affect battery performance is provided in the battery system so as not to come into direct contact with the battery and the electrolyte. As a result, it has been found that the effect of the present invention can be obtained by adding at least one oxide selected from the group consisting of SrO, CaO, BaO, and MgO as an oxide for generating a carbonate. . Japanese Patent Application Laid-Open No. Hei 7-153496 discloses that the cycle characteristics of a battery are improved by adding and mixing an active material and at least one oxide selected from BaO, MgO, and CaO into a positive electrode. However, the present invention does not add and mix at least one oxide selected from SrO, BaO, MgO, and CaO into a positive electrode, but instead uses a solid state such as a powder or a molded body to form an electrode and an electrolytic solution. It is arranged so that it does not come into direct contact with the liquid,
Both have completely different problems, and therefore have different oxide arrangements. Since these oxides react slowly with carbon dioxide to form carbonates and exist stably in the battery system,
It does not cause a decrease in battery performance. With respect to ensuring safety at the time of overcharging as described above, at the time of overcharging, oxygen generation occurs due to decomposition of the positive electrode active material itself in preference to gas generation due to decomposition of the electrolytic solution, and the reaction speed is high when left at high temperature. It is overwhelmingly faster than the gas generation rate. Therefore, the internal pressure of the battery rises and the safety mechanism operates, so that safety against overcharging is ensured. [0015] [Embodiment of the Invention The present invention can be implemented in the form described Motomeko, as described in claim 1, a positive electrode consisting mainly of lithium-containing transition metal oxide, lithium a negative electrode and an active material, a non-aqueous non-aqueous electrolyte secondary battery comprising an electrolytic solution, Sr O a powder or molded body capable of producing carbonate by reacting with carbon dioxide generated in the battery system By arranging it so that it does not come into direct contact with the electrode and electrolyte in a solid state, this oxide can serve as a positive electrode, negative electrode,
When present in the battery system separately from the electrolytic solution, it reacts with carbon dioxide gas generated when the battery is left at a high temperature to generate SrCO 3 . SrCO 3 which generated is relatively inert, stable present in the cell system, does not adversely affect the subsequent battery characteristics. The present invention will be described in detail below with reference to examples. (Example 1) FIG. 1 shows a cutaway perspective view of a cylindrical battery used in this example, a conventional example and a comparative example.
In FIG. 1, reference numeral 1 denotes a negative electrode plate to which a negative electrode lead plate 2 is attached, and 3 denotes a positive electrode plate to which a positive electrode lead plate 4 is attached. The negative electrode plate 1 and the positive electrode plate 3 are housed in a battery case 7 which also serves as a negative electrode terminal with an electrode plate group spirally wound via a separator 5 with insulating plates 6 arranged above and below the electrode plate group. The upper edge of the battery case 7 is sealed via an insulating packing 8 with a sealing plate 9 also serving as a positive electrode terminal provided with a valve.
The inside of the sealing plate 9 is 10 kg / cm 2 at a battery internal pressure of 20 ° C.
Is exceeded, conduction between the positive electrode terminal and the positive electrode lead plate 4 is stopped so that external current is cut off. Hereinafter, a method of manufacturing the positive electrode plate and the negative electrode plate will be described in detail. As the positive electrode active material, LiNi 0.8 Co 0.2 O 2 was used. First, nickel hydroxide, cobalt hydroxide, and lithium hydroxide are mixed at an atomic ratio of Ni: Co: Li of 0.8:
It was weighed so as to be 0.2: 1.0, and was sufficiently mixed by a ball mill. Then, this mixture was put into a crucible made of alumina and heat-treated in oxygen at 750 ° C. for 10 hours. After natural cooling, pulverization and classification were performed to obtain a positive electrode active material powder having an average particle size of about 10 μm. 6 parts by weight of artificial graphite powder was added to 100 parts by weight of this active material, and N-
A solution in which polyvinylidene fluoride (hereinafter, referred to as PVDF) as a binder was dissolved in a solvent of methylpyrrolidone (hereinafter, referred to as NMP) was kneaded to form a paste. The amount of the added PVDF was adjusted to 4 parts by weight with respect to 100 parts by weight of the active material. Next, this paste was applied to both sides of an aluminum foil, dried, and rolled to obtain a positive electrode plate having a thickness of 0.14 mm, a width of 37 mm, and a length of 380 mm. In addition, in producing the positive electrode plate, a series of steps after kneading were performed in dry air. As the negative electrode, a mesophase small sphere having an average particle size of 6.0 μm, which was heat-treated at 2800 ° C. and graphitized, was used. 100 parts by weight of the graphitized mesophase was mixed with 3 parts by weight of styrene / butadiene rubber as a binder, and an aqueous carboxymethyl cellulose solution was added and kneaded to form a paste. This paste is coated on both sides of the copper foil, dried, and rolled to a thickness of 0.20 mm, a width of 39 mm,
A negative electrode plate having a length of 420 mm was used. Then, a lead plate was attached to each of the positive electrode plate and the negative electrode plate, and the thickness was 0.025 mm, the width was 45 mm, and the length was 1
It was spirally wound through a 000 mm separator and housed in a battery case having a diameter of 17.0 mm and a height of 50 mm. As an oxide to be subsequently added, SrO having an average particle size of about 8 μm was added to NMP in the same manner as in the preparation of the positive electrode plate.
A solution obtained by dissolving PVDF as a binder in the above solvent was kneaded to form a paste. This paste was applied to one side of an aluminum foil, dried and rolled, and then punched into a circle having a diameter of 8 mm, and the aluminum foil side was welded to the bottom of the sealing plate. The thickness of the oxide layer was set to 0.08 mm including the thickness of the aluminum foil. Further, the amount of SrO charged is 0.1 to 1 gram of LiNi 0.8 Co 0.2 O 2 , which is a positive electrode active material.
It was 1 mmol. As the electrolyte, ethylene carbonate (hereinafter, referred to as ethylene carbonate)
EC and dimethyl carbonate (hereinafter referred to as DMC) were mixed at a volume ratio of 20:80, and a solution obtained by dissolving 1 mol / liter of LiPF 6 as an electrolyte was injected. At that time, the electrolyte was prevented from contacting the oxide layer disposed on the bottom of the sealing plate. Then, after the electrolyte solution was sufficiently absorbed by the electrode plate group, the battery was sealed to obtain a completed battery, and 20 cells were produced as the battery of Example 1. (Conventional example) A battery was manufactured in exactly the same manner as in Example 1 except that the SrO oxide was not disposed in the battery system, and 20 cells were manufactured as a conventional battery. (Comparative Example) The same amount of SrO powder as in Example 1 was added to the battery system in a state where it was previously mixed in the positive electrode, instead of being arranged at the bottom of the sealing plate. A battery was produced in exactly the same manner as in Example 1 except that SrO was added to the positive electrode, and 20 cells were produced as batteries of the comparative example. The batteries of Example 1, Conventional Example and Comparative Example were subjected to charge / discharge tests. The charging was performed at a constant current voltage, and the battery was charged to 4.2 V at a constant current of 630 mA.
After reaching 2 V, conversion to constant voltage charging was performed, and charging was completed in 2 hours. Discharge was performed at a constant current of 900 mA, and the discharge end voltage was set to 2.5 V. Such charging and discharging is performed for 20
Five cycles were performed in an environment of ° C., and the capacity at the third cycle was used as the initial capacity. Then, the battery in the charged state was left in a thermostat at 85 ° C. for 15 hours. Thereafter, the battery was returned to an environment of 20 ° C. and the conduction of the battery was measured. Thereafter, the battery with conduction was charged and discharged again, and the capacity at the third cycle was taken as the capacity after standing. When the internal pressure of the battery exceeded about 10 kg / cm 2 , the safety mechanism provided in the sealing plate 9 was activated, and the conduction between the positive electrode and the negative electrode was lost. Table 1 shows the results together with the average values of the initial capacity and the capacity after leaving. [Table 1] The battery capacity after being left at a high temperature was measured for a battery in which the safety mechanism did not operate. In the battery of Example 1, all cells remained conductive even after being left at a high temperature, indicating that the safety mechanism was not operating. In other words, it is considered that the internal pressure of the battery has fallen below the predetermined value due to the absorption of the gas generated during the high temperature storage by the SrO provided inside. The battery capacity after high temperature storage is as large as 938 mAh,
It can be seen that the reaction product of SrO does not adversely affect the battery characteristics. On the other hand, in the conventional battery, 15 cells have lost their function as a battery because the safety mechanism has been activated together with an increase in battery internal pressure due to high temperature storage. In addition, in the battery of the comparative example, almost the same 14 cells resulted in the operation of the safety mechanism. Also, the battery capacity tends to be somewhat smaller, which is not preferable. From the above, the purpose of the present invention cannot be achieved by adding and mixing SrO into the positive electrode in order to obtain the effects of the present invention, and the SrO is disposed in the battery system so as not to come into direct contact with the electrode and the electrolytic solution. It turns out to be important. In addition, another 10 batteries similar to the battery of Example 1 were prepared and subjected to an overcharge test at a constant current of 1 A. In all batteries, the safety mechanism was activated after 18 to 20 minutes, and the external current was shut off. No ignition, rupture or white smoke of the battery was observed, and the battery surface temperature was about 50 ° C. In other words, even if SrO is present in the battery system, it is expected that gas absorption at the time of overcharging does not occur or its speed is slow, and the present invention does not impair the safety at the time of overcharging. I understand. REFERENCE EXAMPLE A battery was prepared in which BaO was used in place of SrO as the oxide to be added in the battery of Example 1, and the amount of addition was as shown in Table 2 with respect to 1 gram of the positive electrode active material. And Battery A, Battery B, Battery C, Battery D, Battery E, and Battery F, respectively. These batteries were charged and discharged in the same manner as the battery of Example 1, and left at a high temperature in a charged state. Thereafter, the continuity of the battery was measured, and the results are shown in Table 2. [Table 2] In any of the batteries B, C, D, and E, the safety mechanism does not operate, and the effect of the present invention is obtained. However, in the battery A having a small addition amount of 0.03 mmol, the safety mechanism of about half of the cells was activated, and it can be seen that the suppression of the battery internal pressure was insufficient. On the other hand, even in the battery F having the largest addition amount of 0.25 mmol, a battery in which a part of the safety mechanism was operated was observed.
This is considered to be because the volume of voids in the battery became extremely small due to the increase in the volume of the added BaO, and the rate of increase of the battery internal pressure was faster than the gas absorption reaction, and the safety mechanism was activated. . From these results, it was found that the amount of oxide to be added was 0.0% per gram of the positive electrode active material.
It can be said that it is important that the amount is 4 mmol to 0.20 mmol. Although LiNi 0.8 Co 0.2 O 2 was used as the positive electrode active material in Example 1 and Reference Example , LiNi 0.8 Co 0.2 O 2 was used.
Al or Mn as part of Ni including O 2 as another element
Or a solid solution substituted with B, LiCoO 2 , LiMn 2 O
A similar effect was obtained when 4 was used. The present invention is applicable to a non-aqueous electrolyte secondary battery using a lithium-containing transition metal oxide for a positive electrode. The negative electrode is made of graphitized mesophase spheres. However, other carbon materials such as artificial graphite, cokes, carbon fibers and the like, and lithium such as metal oxides are inserted and released. The present invention can be applied to a nonaqueous electrolyte secondary battery using lithium as an active material, for example, when a lithium alloy or lithium metal is used. As the electrolytic solution, a mixed solvent of EC and DMC was used as a solvent in this embodiment, but other solvents such as cyclic carbonates such as propylene carbonate and butylene carbonate, diethyl carbonate and ethyl carbonate Chain carbonates such as methyl carbonate, 1,2-
Any known compounds such as ethers such as dimethoxyethane and 2-methyltetrahydrofuran can be used alone or as a mixed solvent. LiBF for solute
4 , LiClO 4 and the like can be used. As described above, according to the present invention, the battery function is satisfied by satisfying the battery characteristics, and even when the battery is left at a high temperature in a charged state, the internal pressure of the battery is prevented from rising. Has the advantageous effect of not causing the loss of

【図面の簡単な説明】 【図1】本実施例,従来例,比較例で用いた円筒形電池
の断面切欠斜視図 【符号の説明】 1 負極板 2 負極リード板 3 正極板 4 正極リード板 5 セパレータ 6 絶縁板 7 電池ケース 8 絶縁パッキング 9 封口板
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cutaway perspective view of a cylindrical battery used in the present embodiment, a conventional example, and a comparative example. [Description of References] 1 negative electrode plate 2 negative electrode lead plate 3 positive electrode plate 4 positive electrode lead plate 5 Separator 6 Insulating plate 7 Battery case 8 Insulating packing 9 Sealing plate

フロントページの続き (56)参考文献 特開 平10−255860(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 10/40 H01M 4/02 H01M 10/52 Continuation of the front page (56) References JP-A-10-255860 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) H01M 10/40 H01M 4/02 H01M 10/52

Claims (1)

(57)【特許請求の範囲】 【請求項1】 リチウム含有遷移金属酸化物を主体とす
る正極と、リチウムを活物質とする負極と、非水電解液
とを備えた非水電解液二次電池において、電池系内に発
生する炭酸ガスと反応して炭酸塩を生成し得るSrOを
粉末あるいは成型体など固体の状態で電極および電解液
とは直接接触しないように配置したことを特徴とする非
水電解液二次電池。
(57) [Claim 1] A non-aqueous electrolyte secondary comprising a positive electrode mainly composed of a lithium-containing transition metal oxide, a negative electrode mainly composed of lithium, and a non-aqueous electrolyte. In the battery, SrO capable of reacting with carbon dioxide gas generated in the battery system to form a carbonate is disposed in a solid state such as a powder or a molded body so as not to directly contact the electrode and the electrolyte. Non-aqueous electrolyte secondary battery.
JP20566497A 1997-07-31 1997-07-31 Non-aqueous electrolyte secondary battery Expired - Fee Related JP3533893B2 (en)

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JP4529207B2 (en) 1999-11-30 2010-08-25 ソニー株式会社 Non-aqueous electrolyte battery
US7097943B2 (en) * 2001-01-31 2006-08-29 Korea Institute Of Science And Technology UV-cured multi-component polymer blend electrolyte, lithium secondary battery and their fabrication method
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US7041412B2 (en) 2001-07-23 2006-05-09 Matsushita Electric Industrial Co., Ltd. Non-aqueous electrolyte secondary battery
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