JPH0433263A - Manufacture of electrode composition material - Google Patents
Manufacture of electrode composition materialInfo
- Publication number
- JPH0433263A JPH0433263A JP2137816A JP13781690A JPH0433263A JP H0433263 A JPH0433263 A JP H0433263A JP 2137816 A JP2137816 A JP 2137816A JP 13781690 A JP13781690 A JP 13781690A JP H0433263 A JPH0433263 A JP H0433263A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- powder
- solid electrolyte
- slurry
- electrode composition
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Conductive Materials (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明(よ 固体電池 キャバシ久 センサ、表示素子
、記録素子などの固体の電気化学素子に用いる電極組成
物の製造方法に関すム さらに詳しくζよ ポリアルキ
レンイミンと脂肪酸との脱水縮合反応物であるアミド化
合物を電極活物質粉大固体電解質粉太 熱可塑性樹脂を
含む溶媒中に添加するものである。[Detailed Description of the Invention] Industrial Field of Application The present invention relates to a method for manufacturing an electrode composition used in solid electrochemical elements such as sensors, display elements, and recording elements. An amide compound, which is a dehydration condensation reaction product of an alkylene imine and a fatty acid, is added to a solvent containing an electrode active material, solid electrolyte powder, and thermoplastic resin.
従来の技術
固体電解質を用いることで液漏れがなl、X、小形薄形
化の電池 電気二重層キャパシタなどの固体の電気化学
デバイスを得ることができる。BACKGROUND OF THE INVENTION By using a solid electrolyte, it is possible to obtain solid electrochemical devices such as small and thin batteries, electric double layer capacitors, etc. without liquid leakage.
しかしなか叡 弾性に欠ける固体物質で素子が構成され
ていることか収 機械的衝撃に対してはきわめて脆く、
破損しやすい欠点があaこのような問題を解決するた数
特開昭63−245871号公報にあるようζへ 合
成ゴムなどの熱可塑性樹脂を固体電解質や電極活物質に
混合することで可撓性を付与し 機械的衝撃に対しても
破損しにくい素子が提案されていも この際電極活物
質および固体電解質は電気絶縁性の熱可塑性樹脂と混合
され電極組成物として用いられa発明が解決しようとす
る課題
このような固体電解質粉末 固体電解質粉末および熱可
塑性樹脂よりなる電極組成物は 一般に熱可塑性樹脂を
溶解した溶剤中におのおのの粉末を分散してスラリー状
とし これを成形した後あるいは成形しながら溶剤を散
逸させて得もこの檄 固体電解質粉末はイオン性である
ので人アルコ−)L< アセトンなどの親水性溶剤ま
たは極性溶剤を用いて分散させると固体電解質粉末が前
記溶剤に僅かながら溶解しまた変質するのでトルエンな
どの親油性の非極性溶剤が用いられも 従って、親水性
である固体電解質粉末は二次粒子を形成して熱可塑性樹
脂中に不均一に分散することが多く、電極活物質粉末と
均一に混合されず、とくべ 電極組成物の電気容量を大
きくするために混合する固体電解質粉末の量を少なくし
た場合、電極組成物内で十分なイオン伝導性を保持され
ず、電極の利用率が極端に低下するという問題点かあa
また 均質な大面積の電極組成物を得ることが困難で
あも 本発明はこのような問題点を解決するもので、電
極の利用率が高い均質な電極組成物を得る電極組成物の
製造法を提供することを目的とすム
課題を解決するための手段
上記問題点を解決するため本発明(よ ポリアルキレン
イミンと脂肪酸との脱水縮合反応物であるアミド化合物
を電極活物質粉末 固体電解質粒子、および熱可塑性樹
脂を含む溶媒中に添加するものであ4
作用
このようにして得られる電極組成物(よ ポリアルキレ
ンイミンと脂肪酸との脱水縮合反応物であるアミド化合
物の作用で電極活物質粉末および固体電解質粉末を均一
に混合・分散させるためイオン伝導のための経路が電極
組成物内で均一に構築されることとなも
実施例
以下、本発明の一実施例の電極組成物の製造法を詳細に
説明する力匁 本発明は以下の実施例に限定されるもの
ではな(−また 以下の実施仇比較例において仏 %は
とくに断わらない限り重量区 電量% 重量比を表わす
。However, due to the fact that the device is made of a solid material that lacks elasticity, it is extremely brittle against mechanical shock.
It has the disadvantage of being easily damaged, but the only way to solve this problem is as described in Japanese Patent Application Laid-Open No. 63-245871.By mixing thermoplastic resin such as synthetic rubber with the solid electrolyte and electrode active material, it becomes flexible. Although an element has been proposed that imparts properties and is resistant to damage due to mechanical shock, the electrode active material and the solid electrolyte are mixed with an electrically insulating thermoplastic resin and used as an electrode composition. Such solid electrolyte powders Electrode compositions made of solid electrolyte powders and thermoplastic resins are generally made into a slurry by dispersing each powder in a solvent in which a thermoplastic resin is dissolved, and after molding or molding the slurry. However, the solid electrolyte powder is ionic, so if it is dispersed using a hydrophilic or polar solvent such as acetone, the solid electrolyte powder will dissolve slightly in the solvent. Moreover, lipophilic non-polar solvents such as toluene are used to avoid deterioration in quality. Therefore, hydrophilic solid electrolyte powders often form secondary particles and are unevenly dispersed in thermoplastic resins. In particular, if the amount of solid electrolyte powder mixed in order to increase the capacitance of the electrode composition is reduced, sufficient ionic conductivity may not be maintained within the electrode composition. The problem is that the electrode utilization rate is extremely low.
In addition, even though it is difficult to obtain a homogeneous electrode composition with a large area, the present invention solves such problems and provides a method for producing an electrode composition that yields a homogeneous electrode composition with a high electrode utilization rate. In order to solve the above-mentioned problems, the present invention aims to provide an electrode active material powder using an amide compound, which is a dehydration condensation reaction product of a polyalkylene imine and a fatty acid, and solid electrolyte particles. , and a thermoplastic resin.The action of the electrode composition obtained in this way (the action of the amide compound, which is a dehydration condensation reaction product of polyalkyleneimine and fatty acid) makes the electrode active material powder In order to uniformly mix and disperse the solid electrolyte powder, paths for ion conduction are uniformly constructed within the electrode composition. The present invention is not limited to the following Examples (-Also, in the following Examples and Comparative Examples, % represents a weight ratio unless otherwise specified.
本実施例の電極活物質として(よ 金属鍜 金属級 金
属リチウムなどの単体金KLi−Al、 LaNi5な
どの合金; 硫化臥 硫化机 銅シュブレル化合轍 銀
シュブレル化合法 硫化チタン、硫化ニオブ、硫化モリ
ブデンなどの金属硫化物; 二酸化マンガン、酸化バナ
ジウム 酸化コバルト、酸化クロムなどの金属酸化物;
塩化瓜 ヨウ化舷 フッ化カーボンなどのハロゲン化
物; 活性炭、黒舷カーボンブラックなどの炭素材料な
ど常温で固体状の材料をあげることができも 平均粒径
が1μm以下の超微粒子から数10μmの粒子のものま
で何れも用いることができも
固体電解質粉末としてζ7 MCuaIa−xcli
*x(x−0゜25−1.0. M= Rb、 K、
NHJまたはそれらを混合したモノ)やCuI−Cus
p−Mossガラスなどの銅イオン伝導性固体電解覧R
bAgaIs 、 Ag5Si、 Agl−Ag20−
MoOsガラ7、、 Ag*InWO4などの銀イオ
ン伝導性固体電解覧 Lil、Lil−1hC1,Li
−β−AhOs、Lir−LiaS−BaS3、PE0
−LlCFsSOsなどのリチウムイオン伝導性固体電
解質、Hs Mo+ 2 PO4−・29hQ、 Hs
W+ 2POs・・29H20などのプロトン導性固体
電解質を用いることができも 平均粒径が1μm以下の
超微粒子から数lOμmの粒子のものまで何れも用いる
ことができも 平均粒径が1μm以下の超微粒固体電解
質粉末であっても均一に分散できる。熱可塑性樹脂とし
てit 1,4−ポリブタジェン、天然ゴベ ポリイ
ソプレン、SBR,NBR,SBS、 SIS、
SE B S、 ブチルゴな フォスファゼンゴな
ポリエチレン、ポリプロピレン、ポリエチレンオキシド
、ポリスチレン、 1,2−ポリブタジェン、ポリテト
ラフルオロエチレンなどを使用するのか好ましく−
電極組成物の製造にあたっては分散媒として、n−ヘキ
サン、 n−へブタン、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/l、
、 トリクレンなどの親油性の非吸水性の固体電解質
と反応しない飽和炭化水素系継起 芳香族炭化水素系継
起 ハロゲン化炭化水素継起 エステル系溶剤が用いら
れも
ポリアルキレンイミンと脂肪酸との脱水縮合反応物であ
るアミド化合物を与えるポリアルキルアミンとして、ポ
リエチレンイミン、ポリプロピレンイミン、ポリブチレ
ンイミンなどがあげられる。As the electrode active materials of this example (Metallic grade: Metallic lithium, etc., elemental gold such as KLi-Al, LaNi5, etc. alloy; Sulfurization method: Copper Chevrehl compounding method; Silver Chevrehl compounding method; Titanium sulfide, Niobium sulfide, Molybdenum sulfide, etc.) Metal sulfides; Metal oxides such as manganese dioxide, vanadium oxide, cobalt oxide, chromium oxide;
Halogenated substances such as chloride melon, iodide, and carbon fluoride; Materials that are solid at room temperature, such as activated carbon and carbon materials such as blackboard carbon black; Ultrafine particles with an average particle size of 1 μm or less to particles of several tens of μm. ζ7 MCuaIa-xcli can be used as a solid electrolyte powder.
*x(x-0゜25-1.0. M= Rb, K,
NHJ or a mixture thereof) or CuI-Cus
List of copper ion conductive solid electrolytes such as p-Moss glass
bAgaIs, Ag5Si, Agl-Ag20-
List of silver ion conductive solid electrolytes such as MoOs Gala 7, Ag*InWO4 Lil, Lil-1hC1, Li
-β-AhOs, Lir-LiaS-BaS3, PE0
- Lithium ion conductive solid electrolyte such as LlCFsSOs, Hs Mo+ 2 PO4- 29hQ, Hs
A proton-conducting solid electrolyte such as W+ 2POs...29H20 can be used, or anything from ultrafine particles with an average particle size of 1 μm or less to particles of several 10 μm can be used. Even fine solid electrolyte powder can be uniformly dispersed. As thermoplastic resin it 1,4-polybutadiene, natural gobe polyisoprene, SBR, NBR, SBS, SIS,
SE B S, butylgo na phosphazengo na
It is preferable to use polyethylene, polypropylene, polyethylene oxide, polystyrene, 1,2-polybutadiene, polytetrafluoroethylene, etc. In producing the electrode composition, as a dispersion medium, n-hexane, n-hebutane, n-octane, Cyclohexane, benzene, toluene, xylene, ethyl acetate/l,
, Saturated hydrocarbon series that does not react with lipophilic non-water-absorbing solid electrolytes such as tricrene, Aromatic hydrocarbon series, Halogenated hydrocarbon series, Dehydration condensation reaction product of polyalkylene imine and fatty acid, even when an ester solvent is used. Examples of the polyalkylamine that provides the amide compound include polyethyleneimine, polypropyleneimine, polybutyleneimine, and the like.
これらに相当するアルキレンイミンを酸性触媒中で重合
させることで得られるもので、好ましくは分子中に窒素
原子が8から160個含むポリエチレンイミングがあげ
られも 脂肪酸として番友カプリル観 バルミチン酸
ステアリン醜 オレイン酸、 リノール葭 リシノール
酸などがあげられも ポリアルキレンイミンと脂肪酸を
、窒素気流で撹拌しながら150〜200tで反応生成
分の水を留出しながら縮合することで得ることができも
ポリアルキレンイミンと脂肪酸とのモル比(表1/2か
ら1/80が好ましく℃
このようにして得られたアミド化合物(よ 固体電解質
組成物全量に対1.. 0. 5から20%添加されも
本実施例の電極組成物は次のようにして得られる。熱可
塑性樹脂を親油性の溶剤に溶解し1〜20%の溶液とし
たものく アミド化合物をスラリー全体に対して0.1
〜20%の割合になるように加え 電極活物質粉末と固
体電解質粉末 必要に応じ導電剤粉末と、またはあらか
じめ所定の配合比で電極活物質粉末と固体電解質粉末と
必要に応じ導電剤粉末とを混合した混合物を加えボール
ミ)Lt、 ディスパーサなどの混合粉砕機により粉
砕混合して固形分含量が5〜95%の電極スラリーを調
製すも また(よ ポリエーテル化合物を溶解した親油
性の溶剤に電極活物質粉末と固体電解質粉末 必要に応
じ導電剤粉末と、またはあらかじめ所定の配合比で電極
活物質粉末と固体電解質粉末と必要に応じ導電剤粉末と
を混合した混合物を分散したスラリーと、熱可塑性樹脂
を親油性の溶剤に溶解した溶液とを混合分散することで
電極スラリーを得ることもできも
次善! このようにして得たスラリーをそのまま成蕉
またはテフロン板とかナイロンメツシュシートとかの
支持体上に流延または塗布して成形した後、溶剤を散逸
させることで電極組成物が得られも 支持体がメツシュ
状であれば支持体を一体化したままで電極組成物として
用いることも可能であム
これらの工程(よ 相対湿度が40%以下の乾燥雰囲気
中で行なわれる。好ましくは 露点がマイナス20℃以
下の乾燥した窒素あるいはアルゴン等の不活性ガス雰囲
気中で行なわれる。It is obtained by polymerizing alkylene imines corresponding to these in an acidic catalyst, preferably polyethylene imine containing 8 to 160 nitrogen atoms in the molecule.
Stearin Ugly Oleic acid, linoleic acid, ricinoleic acid, etc. Can be obtained by condensing polyalkylene imine and fatty acid while stirring in a nitrogen stream and distilling off the reaction product water at 150 to 200 tons. The molar ratio of alkyleneimine to fatty acid (Table 1/2 to 1/80 is preferred) The electrode composition of this example is obtained as follows: The thermoplastic resin is dissolved in a lipophilic solvent to form a 1 to 20% solution.The amide compound is added at 0.1% to the entire slurry.
Electrode active material powder, solid electrolyte powder, and conductive agent powder if necessary, or electrode active material powder, solid electrolyte powder, and conductive agent powder if necessary in a predetermined mixing ratio. The mixed mixture is added to a lipophilic solvent in which a polyether compound is dissolved, and the electrode slurry is prepared by pulverizing and mixing using a mixing grinder such as a disperser. Active material powder and solid electrolyte powder A slurry in which a mixture of electrode active material powder, solid electrolyte powder, and conductive agent powder as necessary is dispersed, or a mixture of electrode active material powder, solid electrolyte powder, and conductive agent powder as necessary in a predetermined mixing ratio, and thermoplastic It is also possible to obtain an electrode slurry by mixing and dispersing a solution of the resin in a lipophilic solvent, but this is the next best option! The slurry obtained in this way can be used as is, or it can be supported with a Teflon plate or nylon mesh sheet. An electrode composition can be obtained by dissipating the solvent after casting or coating on a body and molding it.If the support is mesh-like, it is also possible to use the support as an electrode composition with the support integrated. These steps are carried out in a dry atmosphere with a relative humidity of 40% or less. Preferably, they are carried out in a dry inert gas atmosphere such as nitrogen or argon with a dew point of -20°C or less.
(実施例1)
熱可塑性樹脂であり結着剤として作用する低密度ポリエ
チレン(エフセレンVL−200、密度=0.9、住人
化学工業製)をトルエンに溶解し10%のポリエチレン
溶液を調整し九 窒素原子を120個含むポリエチレン
イミンとオレイン酸とを1/20のモル比で縮合して得
られたアミド化合物をトルエンに溶解し20%のアミド
化合物溶液(A)を調整した アミド化合物溶液(A)
へ 固形分含量が50%となるように平均粒径が1μm
の銅イオン伝導性固体電解質粉末(RbCu411、s
C1$、’+ 密度=4.7)と平均粒径が0.8μ
mの銅シュブレル相化合物(CuaMoaSv、s。(Example 1) Low-density polyethylene (Efselen VL-200, density = 0.9, manufactured by Sumima Kagaku Kogyo), which is a thermoplastic resin and acts as a binder, was dissolved in toluene to prepare a 10% polyethylene solution. An amide compound obtained by condensing polyethyleneimine containing 120 nitrogen atoms and oleic acid at a molar ratio of 1/20 was dissolved in toluene to prepare a 20% amide compound solution (A). )
The average particle size is 1 μm so that the solid content is 50%.
Copper ion conductive solid electrolyte powder (RbCu411, s
C1$, '+ density = 4.7) and average particle size is 0.8μ
CuaMoaSv, s.
密度= 5.8)との2:1の混合物を分散させた衡ポ
リエチレン溶液を加え固形分含量が50%の電極粉末分
散液(B)を得九 な耘 前記銅イオン伝導性固体電解
質は 所定量のRbC1,CuI、 CuC1よりなる
混合物を200℃で17時間密閉ガラス容器中で加熱反
応することで得九 また 銅シュブレル相化合物+L
MoS2. Cu、 Sの混合物を真空中で1000
℃で48時間加熱反応することで得九所定量のポリエー
テル溶液(A)と電極粉末分散液(B)とトルエンを混
合したの板 アルミナ製のボールミル中で24時間混合
粉砕して電極粉末のスラリーを得島 前記スラリーを平
滑なテフロン製の板の上でドクターブレードを用い塗布
した後、 80℃の乾燥窒素中で5時間乾燥し大きさ8
0x80mm、 厚さ154±5μmの電極粉末含量
が85容積%のシート状の電極成形体(B1)を得t4
(比較例1)
固体電解質分散液(B)の代わりにポリエーテルを含ま
ない電極粉末分散液(C)を用いた以外は実施例1と同
様にして電極粉末含量が85容積%のシート状の電極成
形体(C1)を得九(実施例2)
電極粉末として銀イオン伝導性の平均粒径が8μmのA
ga14WO4粉末と平均粒径が10μmのバナジン酸
銀粉末(Agv 、〒Ve Os )との3=2の混合
物を用(\ 窒素原子を56個含むポリエチレンイミン
とカプリル酸とを1/8のモル比で縮合して得られたア
ミド化合物を含む電極粉末分散液(D)を用いた以外(
上 実施例1と同様にして電極粉末含量が90容量%で
ある厚みが120±8μmの電極組成物(DI)を得た
すK AgeI4WOd;L。An electrode powder dispersion (B) with a solid content of 50% was obtained by adding a balanced polyethylene solution in which a 2:1 mixture of copper ion conductive solid electrolyte (density = 5.8) was dispersed. Obtained by heating a mixture consisting of quantitative amounts of RbC1, CuI, and CuC1 at 200°C for 17 hours in a closed glass container.
MoS2. A mixture of Cu, S and 1000
A plate containing a predetermined amount of polyether solution (A), electrode powder dispersion (B), and toluene mixed together by heating and reacting at ℃ for 48 hours. Mixed and pulverized for 24 hours in an alumina ball mill to obtain electrode powder. Obtaining slurry After applying the slurry using a doctor blade on a smooth Teflon plate, drying it in dry nitrogen at 80°C for 5 hours to obtain a size 8
A sheet-shaped electrode molded body (B1) with a size of 0x80 mm and a thickness of 154 ± 5 μm and an electrode powder content of 85% by volume was obtained t4 (Comparative Example 1) Electrode powder not containing polyether was used instead of the solid electrolyte dispersion (B). A sheet-like electrode molded body (C1) having an electrode powder content of 85% by volume was obtained in the same manner as in Example 1 except that the dispersion liquid (C) was used. (Example 2) Silver ion conductive material was used as the electrode powder. A with an average particle size of 8 μm
A 3=2 mixture of ga14WO4 powder and silver vanadate powder (Agv, Ve Os) with an average particle size of 10 μm was used (\ polyethyleneimine containing 56 nitrogen atoms and caprylic acid at a molar ratio of 1/8). Except for using an electrode powder dispersion (D) containing an amide compound obtained by condensation with (
KAgeI4WOd; L. An electrode composition (DI) having a thickness of 120±8 μm and having an electrode powder content of 90% by volume was obtained in the same manner as in Example 1.
AgeO,AgI、10gを所定の割合で混合し400
tで大気中で6時間加熱反応することで得九 ま?Q
Ags、yV*osはAg粉末とV*Osを所定の割
合で混合し 封管中で550℃で6時間加熱反応するこ
とで得九(比較例2)
電極粉末分散液(D)の代わりにアミド化合物を含まな
い電極粉末分散液(E)を用いた以外は実施例2と同様
にして電極粉末含量が90容積%のシート状の電極成形
体(El)を得た(実施例3)
電極粉末として、 リチウムイオン伝導性の平均粒径が
5μmのLiI−HaO粉末と平均粒径が6μmの硫化
ニオブ粉末(NbSp)との1=1の混合物を用−入
窒素原子を40個含むポリプロピレンイミンとオレイン
酸とを1/10のモル比で縮合して得られたアミド化合
物を含む電極粉末分散液(F)を用いた以外(よ 実施
例1と同様にして電極粉末含量が90容積%である厚み
が85±5μmの電極成形体(F1〕を得た な耘 L
iI・I20. Nb5aは市販の試莞をエチルエーテ
ル中でボールミルにより粉砕したものを用い九
(比較例3)
電極粉末分散液(F)の代わりにアミド化合物を含まな
い電極粉末分散液(G)を用いた以外は実施例3と同様
にして電極粉末含量が90容積%のシート状の電極成形
体(G1)を得た以下に述べる方法により電極成形体の
特性評価を行なった
実施例1〜3、比較例1〜3で得られた電極組成物を直
径10mmの円板状におのおの20枚づつ打ち抜き特性
試験用の試料とし九 実施例1および比較例1の電極円
板について、固体電解質としてRbCu4I+、5C1
s、r、粉末1grを200 kg/cm2の圧力で成
形した直径10mmのペレットを挟む形で上下に1枚づ
つ配置しさらにその上下に白金円板を配置した後 全体
を50に、g/cm2の圧力で上下から加圧した状態で
、窒素ガス雰囲気中で130℃で3時間加熱し試験電池
B2(実施例1)およびC2(比較例1)を組み立て島
実施例2および比較例2の電極円板について(上 固
体電解質としてAgs I4WO4粉末を用いて同様に
試験電池D2 (実施例2)およびF2(比較例2)
を組み立てた 実施例3および比較例3の電極円板につ
いて(友 固体電解質としてLil−I20粉末を用t
、X。Mix 10g of AgeO and AgI in a predetermined ratio and make 400
9 obtained by heating reaction in the atmosphere for 6 hours at t? Q
Ags, yV*os can be obtained by mixing Ag powder and V*Os at a predetermined ratio and heating and reacting in a sealed tube at 550°C for 6 hours (Comparative Example 2) Instead of electrode powder dispersion (D) A sheet-shaped electrode molded body (El) having an electrode powder content of 90% by volume was obtained in the same manner as in Example 2 except that an electrode powder dispersion (E) containing no amide compound was used (Example 3) Electrode As a powder, a 1=1 mixture of lithium ion conductive LiI-HaO powder with an average particle size of 5 μm and niobium sulfide powder (NbSp) with an average particle size of 6 μm was used.
Example 1 was carried out in the same manner as in Example 1 except that an electrode powder dispersion (F) containing an amide compound obtained by condensing polypropylene imine containing 40 nitrogen atoms and oleic acid at a molar ratio of 1/10 was used. An electrode molded body (F1) with a thickness of 85 ± 5 μm and an electrode powder content of 90% by volume was obtained.
iI・I20. Nb5a was obtained by pulverizing a commercially available test tube in ethyl ether using a ball mill (Comparative Example 3) Except for using an electrode powder dispersion (G) that does not contain an amide compound instead of the electrode powder dispersion (F). A sheet-like electrode molded body (G1) with an electrode powder content of 90% by volume was obtained in the same manner as in Example 3. Characteristics of the electrode molded body were evaluated by the method described below. Examples 1 to 3 and Comparative Example The electrode compositions obtained in 1 to 3 were punched out into 20 discs each with a diameter of 10 mm and used as samples for characteristic testing.9 For the electrode discs of Example 1 and Comparative Example 1, RbCu4I+ and 5C1 were used as solid electrolytes.
S, R, 1g of powder was molded at a pressure of 200 kg/cm2, and one pellet with a diameter of 10mm was placed on the top and bottom, and platinum disks were placed on top and bottom of the pellets. Test batteries B2 (Example 1) and C2 (Comparative Example 1) were assembled by heating at 130°C for 3 hours in a nitrogen gas atmosphere under pressure applied from above and below. Regarding the disk (top) Similarly test batteries D2 (Example 2) and F2 (Comparative Example 2) using Ags I4WO4 powder as solid electrolyte
Regarding the electrode disks of Example 3 and Comparative Example 3, which were assembled using Lil-I20 powder as the solid electrolyte,
,X.
負極として厚さ0.3mrrI、直径10mmのリチウ
ム円板を用い試験電池F2(実施例3)およびG2
(比較例3)を組み立てf、F2およびG2については
加圧のみで加熱は行わなかった おのおの同じものを1
0個づつ組み立てtラ 試験電池B2、C2について
、 0.6Vの一定電圧テ17時間充電した後、 1m
Aの一定電流で10秒間放電を行なuX、放電直前およ
び放電直後の電池電圧の差(分極)を測定し10個の電
池について平均値と標準偏差値を求めた また 同じ電
流値で0゜3ボルトまで連続放電を行ない放電容量を求
へ理論容量(100%)に対する電極活物質の利用率を
求めた 試験電池D2、F2については0゜50Vの一
定電圧で17時間充電&200μAの一定電流値で10
秒間放電し分極の平均値と標準偏差値を求めち また
同じ電流値で0.3Vまで連続放電を行い理論容量(1
00%)に対する電極活物質の利用率を求めた 試験電
池F2およびG2については 50μAの一定電流で1
0秒間放電し分極の平均値と標準偏差値を求めたまた
同じ電流値で1. Ovまで連続放電を行い理論容量(
100%)に対する電極活物質の利用率を求め九 分極
値の結果を第1褒 利用率の結果を第2表に示す。また
電極成形体の曲げ強度を、長さ4.0mm幅5mmの
組成物を半径が50mmの曲面に沿って1秒間に2回の
割合で繰り返し折り曲げた賑 破断にいたるまでの回数
で評価し九 結果を第3表に示す。以上の測定値は何
れも2
0℃での値である。Test batteries F2 (Example 3) and G2 were prepared using a lithium disk with a thickness of 0.3 mrrI and a diameter of 10 mm as the negative electrode.
(Comparative Example 3) was assembled, and for f, F2 and G2, only pressure was applied but no heating was performed.
Assemble 0 pieces at a time For test batteries B2 and C2, after charging at a constant voltage of 0.6V for 17 hours, 1m
Discharge was performed for 10 seconds at a constant current of A, uX, and the difference (polarization) between battery voltages immediately before and after discharge was measured, and the average value and standard deviation value were calculated for 10 batteries.Also, at the same current value, 0° Continuous discharge was performed up to 3 volts to determine the discharge capacity, and the utilization rate of the electrode active material with respect to the theoretical capacity (100%) was determined. Test batteries D2 and F2 were charged for 17 hours at a constant voltage of 0.50 V and a constant current value of 200 μA. So 10
Discharge for seconds and calculate the average value and standard deviation of polarization.
The theoretical capacity (1
For test batteries F2 and G2, the utilization rate of the electrode active material was determined for 0.00%) at a constant current of 50 μA.
After discharging for 0 seconds, the average value and standard deviation of polarization were calculated.
1 at the same current value. Continuously discharge to Ov and theoretical capacity (
100%) of the electrode active material.9 The results of the polarization value are shown in Table 1.The results of the usage rate are shown in Table 2. In addition, the bending strength of the electrode molded body was evaluated by the number of times it took to break when a composition with a length of 4.0 mm and a width of 5 mm was repeatedly bent at a rate of 2 times per second along a curved surface with a radius of 50 mm. The results are shown in Table 3. All of the above measured values are at 20°C.
第2表 利用率
B2 実施例190
C2比較例182
B2 実施例279
B2 比較例269
F2 実施例378
G2 比較例358
*理論容量を100%とし九
第3表 機械強度
電池 機械強度”
B2 実施例1 125
C2比較例1 100
D2 実施例2 130
E2 比較例2 100
F2 実施例3135
G2 比較例3100
本対応する比較例の曲げ強度を1
0としへ
第1表から第3表に示した結果から明らかなように 本
実施例による電極組成物源 比較例に較べ電極利用率は
高く、分極の標準偏差値は小さく電極活物質と電解質と
が均一に混合された均質な電極組成物であることがわか
る。また 分極の平均値も小さ1.% さら圏 機械
的強度を比較すると、本実施例の電極組成物は従来のも
のに比べ大きな強度を与えも
発明の効果
以上の実施例の説明で明かなように 本発明の電極組成
物の製造法によれ(L ポリアルキレンイミンと脂肪酸
との脱水縮合反応物であるアミド化合物の界面活性作用
により長期間安定な電極スラリーを得ることができ、
このスラリーから溶媒を除去し固形化することで均質な
電極組成物を得ることができも また 分極の小さい電
極組成物が得られるという効果がある。Table 2 Utilization rate B2 Example 190 C2 Comparative example 182 B2 Example 279 B2 Comparative example 269 F2 Example 378 G2 Comparative example 358 *Theoretical capacity is 100% Table 3 Mechanical strength battery Mechanical strength B2 Example 1 125 C2 Comparative Example 1 100 D2 Example 2 130 E2 Comparative Example 2 100 F2 Example 3135 G2 Comparative Example 3100 It is clear from the results shown in Tables 1 to 3 that the bending strength of the corresponding comparative example is 10. As shown, the electrode composition source according to this example has a higher electrode utilization rate than the comparative example, and the standard deviation of polarization is small, indicating that the electrode composition is a homogeneous electrode composition in which the electrode active material and electrolyte are evenly mixed. In addition, the average value of polarization is also small (1.%).Also, when comparing the mechanical strength, the electrode composition of this example has greater strength than the conventional one, but it is clear from the description of the example that the effect exceeds that of the invention. According to the method for producing an electrode composition of the present invention (L), it is possible to obtain an electrode slurry that is stable for a long period of time due to the surface active action of the amide compound, which is a dehydration condensation reaction product of polyalkylene imine and fatty acid.
By removing the solvent from this slurry and solidifying it, a homogeneous electrode composition can be obtained, and an electrode composition with low polarization can also be obtained.
イー(゛ミE2\19ノミ2.ρ\ C5ぐJ、
’FF−神セ ゝ;111:2q〒 −’fX−rE−
・lづヒ。E (゛mi E2\19 flea 2.ρ\ C5guJ,
'FF-God Se ゝ;111:2q〒 -'fX-rE-
・lzuhi.
Claims (1)
固体電解質粉末を分散しスラリー状とする工程、および
前記スラリーから溶媒を除く工程を電極組成物の製造法
において、前記スラリー中に、ポリアルキレンイミンと
脂肪酸との脱水縮合反応物であるアミド化合物を添加す
る電極組成物の製造法。The method for producing an electrode composition includes a step of dispersing an electrode active material powder and a solid electrolyte powder in a solvent in which a thermoplastic resin is dissolved to form a slurry, and a step of removing the solvent from the slurry. A method for producing an electrode composition by adding an amide compound which is a dehydration condensation reaction product of imine and fatty acid.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2137816A JPH0433263A (en) | 1990-05-28 | 1990-05-28 | Manufacture of electrode composition material |
| US07/706,234 US5190695A (en) | 1990-05-28 | 1991-05-28 | Methods to produce solid electrolyte and solid electrode composites |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2137816A JPH0433263A (en) | 1990-05-28 | 1990-05-28 | Manufacture of electrode composition material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0433263A true JPH0433263A (en) | 1992-02-04 |
Family
ID=15207526
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2137816A Pending JPH0433263A (en) | 1990-05-28 | 1990-05-28 | Manufacture of electrode composition material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0433263A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006032232A (en) * | 2004-07-20 | 2006-02-02 | Sanyo Electric Co Ltd | Nonaqueous electrolyte secondary battery |
| US7976975B2 (en) | 2006-09-05 | 2011-07-12 | Seiko Epson Corporation | Battery device and electronic apparatus |
| JP2011198755A (en) * | 2010-02-23 | 2011-10-06 | Dowa Electronics Materials Co Ltd | Battery positive electrode material and method of manufacturing the same |
| US10566651B2 (en) | 2014-03-28 | 2020-02-18 | Fujifilm Corporation | All-solid-state secondary battery, solid electrolyte composition and electrode sheet for batteries used in the same, and manufacturing method of electrode sheet for batteries and all-solid-state secondary battery |
-
1990
- 1990-05-28 JP JP2137816A patent/JPH0433263A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006032232A (en) * | 2004-07-20 | 2006-02-02 | Sanyo Electric Co Ltd | Nonaqueous electrolyte secondary battery |
| US7976975B2 (en) | 2006-09-05 | 2011-07-12 | Seiko Epson Corporation | Battery device and electronic apparatus |
| JP2011198755A (en) * | 2010-02-23 | 2011-10-06 | Dowa Electronics Materials Co Ltd | Battery positive electrode material and method of manufacturing the same |
| US10566651B2 (en) | 2014-03-28 | 2020-02-18 | Fujifilm Corporation | All-solid-state secondary battery, solid electrolyte composition and electrode sheet for batteries used in the same, and manufacturing method of electrode sheet for batteries and all-solid-state secondary battery |
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