JPH0433255A - Manufacturing method of electrode composition - Google Patents
Manufacturing method of electrode compositionInfo
- Publication number
- JPH0433255A JPH0433255A JP2137812A JP13781290A JPH0433255A JP H0433255 A JPH0433255 A JP H0433255A JP 2137812 A JP2137812 A JP 2137812A JP 13781290 A JP13781290 A JP 13781290A JP H0433255 A JPH0433255 A JP H0433255A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- powder
- solid electrolyte
- electrode composition
- slurry
- 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
-
- Y02E60/12—
Landscapes
- Battery Electrode And Active Subsutance (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Electric Double-Layer Capacitors Or The Like (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
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 エチレンオ
キサイド(EO)鎖および/またはプロピレンオキサイ
ド(PO)鎖を含むカチオン界面活性剤を電極活物質粉
末 固体電解質粉末 熱可塑性樹脂を含む溶媒中に添加
するものであa
従来の技術
固体電解質を用いることで液漏れがなく、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。[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. A cationic surfactant containing an oxide (EO) chain and/or a propylene oxide (PO) chain is added to a solvent containing an electrode active material powder, a solid electrolyte powder, and a thermoplastic resin.a Conventional technology: Using a solid electrolyte It is possible to obtain solid electrochemical devices such as small and thin batteries and electric double layer capacitors without 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る。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.
このような問題を解決するたム 特開昭63−2458
71号公報にあるように 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 この除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
られる。A method to solve such problems: Japanese Patent Application Laid-Open No. 63-2458
As stated in Publication No. 71, although it has been proposed that a thermoplastic resin such as synthetic rubber be mixed with a solid electrolyte or an electrode active material to give it flexibility and resist damage even under mechanical shock, this exception has been proposed. The electrode active material and the solid electrolyte are mixed with an electrically insulating thermoplastic resin and used as an electrode composition.
発明が解決しようとする課題
このような電極活物質粉末 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(よ 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 これを成形した後または成形しながら溶剤を
散逸させて得も この際 固体電解質粉末はイオン性
であるので人アルコ−k 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、とくに 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が保持され
ず、電極の利用率が極端に低下するという問題点かあも
また 均質な大面積の電極組成物を得ることが困難で
あム 本発明はこのような問題点を解決するもので、均
質な柔軟性と機械的強度の優れた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も
課題を解決するための手段
このような課題を解決するため本発明の電極組成物の製
造法ζよ 熱可塑性樹脂を溶解した溶媒中に 電極活物
質粉末および固体電解質粉末を分散してスラリー状とす
る工程および前記スラリーから溶媒を除く工程を含む電
極組成物の製造法において、前記スラリー中にエチレン
オキサイド鎖およびプロピレンオキサイド鎖を有するカ
チオン界面活性剤、 またはエチレンオキサイド机 プ
ロピレンオキサイド鎖のいづれか一方の界面活剤を添加
するものであも
作用
このようにして得られる電極組成物ζ上 エチレンオキ
サイド(EO)鎖および/またはプロピレンオキサイド
(PO)鎖を有するカチオン界面活性剤の作用で電極活
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ム
実施例
以下、本発明の一実施例の電極組成物の製造法をさらに
詳細に説明する力(本発明は以下の実施例に限定される
ものではなuXo また 以下の実施例1 比較例
において訊 %はとくに断わらない限り重量服 重量鳳
重量比を表わす。Problems to be Solved by the Invention Electrode active material powders such as these include electrode compositions consisting of solid electrolyte powders and thermoplastic resins (generally, each powder is dispersed in a solvent in which a thermoplastic resin is dissolved to form a slurry). It is also advantageous to dissipate the solvent after or during molding.In this case, since the solid electrolyte powder is ionic, dispersion using a hydrophilic or polar solvent such as acetone can cause the solid electrolyte powder to Even if lipophilic non-polar solvents such as toluene are used, the hydrophilic solid electrolyte powder forms secondary particles and is unevenly dispersed in the thermoplastic resin because it slightly dissolves in the solvent and changes its quality. In many cases, the solid electrolyte powder is not mixed uniformly with the electrode active material powder, and sufficient ionic conductivity cannot be maintained within the electrode composition, especially when the amount of solid electrolyte powder mixed is reduced in order to increase the capacitance of the electrode composition. In addition, it is difficult to obtain a homogeneous large-area electrode composition.The present invention solves these problems. An object of the present invention is to provide a method for producing an electrode composition that obtains an electrode composition with excellent flexibility and mechanical strength. A method for producing an electrode composition, which 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 cationic surfactant having an ethylene oxide chain and a propylene oxide chain, or a surfactant having either an ethylene oxide chain or a propylene oxide chain may be added to the slurry. Top: Because the electrode active material powder and solid electrolyte powder are uniformly mixed and dispersed by the action of the cationic surfactant having ethylene oxide (EO) chains and/or propylene oxide (PO) chains, the path for ion conduction is determined by the electrode composition. Example The following is a more detailed explanation of the method of manufacturing an electrode composition according to an example of the present invention (the present invention is not limited to the following example). Also, in the following Examples 1 and Comparative Examples, % represents a weight ratio unless otherwise specified.
本実施例の電極活物質としては 金属銚 金属瓜 金属
リチウムなどの単体金KLi−AI、 LaN1r。The electrode active materials of this example include elemental gold such as metal lithium, KLi-AI, and LaN1r.
などの合金: 硫化鉱 硫化鉱 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
ナジウヘ 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は MCu4I2−xc1s+x
(x=0.25−1.0. M−Rb、 K、 NHa
またはそれらを混合したもの)やCul−Cu20−M
oOsガラスなどの銅イオン伝導性固体電解質、RbA
g4I5、Ag5Si、Agl−Ag20−MoOsガ
ラ入AgalaWOaなどの銀イオン伝導性固体電解質
、LiI、LiI−HaQ、 Li−β−A1203
、LiI−LiaS−B2Sa、PE0−L1CFsS
O3などのリチウムイオン伝導性固体電解質、Ha M
o+ 2POa−・29H20゜Hs L t PO4
−・29HaO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
10μmの粒子のものまで何れも用いることができる。Alloys such as: Sulfide ore Sulfide ore Copper Chevrel compound track
Silver Chevrellization method Metal sulfides such as titanium sulfide, niobium sulfide, and molybdenum sulfide: Manganese dioxide, vanadium oxide Metal oxides such as cobalt oxide and chromium oxide: Melon chloride Iodide halides such as carbon fluoride; Activated carbon, black Materials that are solid at room temperature, such as carbon materials such as carbon black, can be used, and anything from ultrafine particles with an average particle size of 1 μm or less to particles of several tens of μm can be used, but the solid electrolyte powder is MCu4I2. -xc1s+x
(x=0.25-1.0. M-Rb, K, NHa
or a mixture thereof) or Cul-Cu20-M
Copper ion conductive solid electrolyte such as oOs glass, RbA
Silver ion conductive solid electrolytes such as g4I5, Ag5Si, Agl-Ag20-MoOs glass-containing AgalaWOa, LiI, LiI-HaQ, Li-β-A1203
, LiI-LiaS-B2Sa, PE0-L1CFsS
Lithium ion conductive solid electrolytes such as O3, HaM
o+ 2POa-・29H20゜Hs L t PO4
Although a proton-conducting solid electrolyte such as -.29HaO can be used, any particle having an average particle size from ultrafine particles of 1 μm or less to particles of several tens of μm can be used.
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ム 熱可塑性樹脂としてl;&
1,4−ポリブタジェン、天然ゴへ ポリイソプレン
、SBR,NBR。Even ultrafine solid electrolyte powder with an average particle size of 1 μm or less can be uniformly dispersed.
1,4-polybutadiene, natural rubber, polyisoprene, SBR, NBR.
SBS、 SIS、 5EBS、 プチルゴへ
フオスファゼンゴ入 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
るのが好ましくl
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−ヘプタン、n−オクタン、 シクロヘキサ
ン、ベンゼン、 トルエン、キシレン、酢酸エチ、+k
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溶剋 芳香族炭化水素系溶剋
ハロゲン化炭化水素溶剋 エステル系溶剤が用いられ
も
EO鎖および/またはPO鎖を有するカチオン界面活性
剤としては 例えば下式(1)または(2)で示される
もの挙げられも
式東 xは窒素または燐; Yは硫黄; A−はC1−
Brド、 F−、ClO4−、CHsCOO−、Cha
os−、OH−、CHsSOs−、AlCl4−、 B
Fi−、PF*−、N0a−またはこれらの組合せ;R
1、R2、RsS R,の少なくとも一つはEO鎖およ
び/またはPO鎖を有する置換基を有するかまたは有し
ない炭素数1から30個の炭化水素基であり、残りは置
換基を有するかまたは有しない炭素数1から30個の同
じまたは異なる炭化水素基であ、L EO鎖および
/またはPO鎖の付加モル数は1から50が好ましt〜
前記カチオン界面活性剤の添加量c& 固体電解質組
成物全量に対し 0.5から20%が好まし1、X。SBS, SIS, 5EBS, to Petilgo
Contains phosphazengo polyethylene, polypropylene,
It is preferable to use polyethylene oxide, polystyrene, 1,2-polybutadiene, polytetrafluoroethylene, etc. In the production of the electrode composition, n-hexane, n-heptane, n-octane, cyclohexane, benzene, Toluene, xylene, ethyl acetate, +k
Saturated hydrocarbon solvents that do not react with lipophilic non-water-absorbing solid electrolytes such as trichlene, aromatic hydrocarbon solvents, halogenated hydrocarbon solvents, and ester solvents that have EO chains and/or PO chains. Examples of cationic surfactants include those represented by the following formula (1) or (2): x is nitrogen or phosphorus; Y is sulfur; A- is C1-
Brdo, F-, ClO4-, CHsCOO-, Cha
os-, OH-, CHsSOs-, AlCl4-, B
Fi-, PF*-, N0a- or a combination thereof; R
At least one of 1, R2, RsS R, is a hydrocarbon group having 1 to 30 carbon atoms with or without a substituent having an EO chain and/or a PO chain, and the rest have a substituent or is the same or different hydrocarbon group having 1 to 30 carbon atoms, and the number of moles of L EO chain and/or PO chain added is preferably 1 to 50.
The amount of the cationic surfactant added is preferably 0.5 to 20% based on the total amount of the solid electrolyte composition.
本実施例の電極組成物は次のようにして得られム 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 EO鎖および/またはPO鎖を有するカチオ
ン界面活性剤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ノにデ
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i戴
EO鎖および/またはPO鎮を有するカチオン界面活
性剤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
次く このようにして得たスラリーをそのまま成慇 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
体上に流延あるいは塗布して成形した徴 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も
これらの工程は 相対湿度が40%以下の乾燥雰囲気中
で行なわれも 好ましくζ友 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などの不活性ガス
雰囲気中で行なわれも(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 式(3)で示されるカチオン界面活
性剤をトルエンに溶解し20%のカチオン界面活性剤溶
液(A)を調整した カチオン界面活性剤溶液(A)
に 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(RbCu4I+、5
C1s、s。The electrode composition of this example was obtained as follows: A thermoplastic resin was dissolved in a lipophilic solvent to form a 1 to 20% solution. A cationic surfactant having an EO chain and/or a PO chain. 0 for the entire slurry. 1-20%
Electrode active material powder, solid electrolyte powder, and conductive agent powder if necessary, or a mixture of electrode active material powder, solid electrolyte powder, and conductive agent powder if necessary in a predetermined mixing ratio. An electrode slurry with a solids content of 5 to 95% is prepared by grinding and mixing using a mixing grinder such as a disperser. A mixture of electrode active material powder, solid electrolyte powder, and conductive agent powder if necessary, or a mixture of electrode active material powder, solid electrolyte powder, and conductive agent powder if necessary in a predetermined mixing ratio was dispersed in an oil-based solvent. Electrode slurry can also be obtained by mixing and dispersing the slurry and a solution of thermoplastic resin dissolved in a lipophilic solvent. Although the electrode composition can be obtained by dissipating the solvent when molded by casting or coating on a support such as a sheet, if the support is in the form of a mesh, it can be used as an electrode composition with the support integrated. Although it is possible, these steps should be carried out in a dry atmosphere with a relative humidity of 40% or less, but preferably with a dew point of -20°C.
(Example 1) Low-density polyethylene (Efselen VL-200, density = 0.9, density = 0.9, thermoplastic resin and binder) (manufactured by Kagaku Kogyo) in toluene to prepare a 10% polyethylene solution, and the cationic surfactant represented by formula (3) was dissolved in toluene to prepare a 20% cationic surfactant solution (A). Activator solution (A)
The average particle size is 1 μm so that the solid content is 50%.
Copper ion conductive solid electrolyte powder (RbCu4I+, 5
C1s, s.
密度= 4.7)と平均粒径が0.8μmの銅シュブレ
ル相化合物(Cu2MOeS)、 e、密度= 5.8
)との2:1の混合物を分散させた後、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f;L MO82、
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へ
所定量のカチオン界面活性剤溶液(A)と電極粉末分散
液(B)とトルエンを混合したの敷 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スラリーを得
な この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樵 80℃の乾燥窒素中で5
時間乾燥し大きさ80x80mm、 厚さ154±5
μmの電極粉末含量が85容積%のシート状の電極成形
体(Bl)を得九
ある厚みが125±10μmの電極成形体(D 1)を
得た な耘 Ag・IaWOajよ Ag*O,A
gI、 WOsを所定の割合で混合し400℃で大気中
で6時間加熱反応することで得九 ま?Q Ags、
yVaOs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た
(比較例1)
固体電解質分散液(B)の代わりにカチオン界面活性剤
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tも(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
ge I4 WO4粉末と平均粒径が10μmのバナジ
ン酸銀粉末(Ags、yVgOs)とノコ:2ノ混合物
を用(\ 式(4)で示されるカチオン界面活性剤を含
む電極粉末分散液(D)を用いた以外は 実施例1と同
様にして電極粉末含量が90容積%で(比較例2)
電極粉末分散液(D)の代わりにカチオン界面活性剤を
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5
μmのLil−H20粉末と平均粒径が6μmの硫化ニ
オブ粉末(NbS* )との1:1の混合物を用(\
式(5)で示されるカチオン界面活性剤を含む電極粉末
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(Fl)を得九 な耘LiI・H2O,N
bS2は市販の試薬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tも
(比較例3)
電極粉末分散液(F)の代わりにカチオン界面活性剤を
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)を得九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で得られた電極成形体を直
径10mmの円板状におのおの20枚づつ打ち抜き特性
試験用の試料とした 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+、6C
1s、s粉末1grを200 kg/cm”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50kg/cm”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B
2(実施例1)およびC2(比較例1)を組み立て九
実施例2および比較例2の電極円板についてc′!、
、固体電解質としてAge Ia 104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
)を組み立て九 実施例3および比較例3の電極円板
についてζよ 固体電解質としてLiI・HeO粉末を
用1、X、負極として厚さ0.3m亀 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G
2 (比較例3)を組み立て九 F2およびG2につ
いては加圧のみで加熱は行なわなかつ九 おのおの同じ
ものを10個づつ組み立てた試験電池B2、C2につい
て、 0.6Vの一定電圧で17時間充電したalmA
の一定電流で10秒間放電を行なし\ 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九 また 同じ電流
値で0.3vまで連続放電を行い放電容量を求へ 理論
容量(100%)に対する電極活物質の利用率を求め九
試験電池D2、B2については0.50Vの一定電圧
で17時間充電比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た また 同じ
電流値で0、3V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 試験電池
F2およびG2について(よ 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九 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表、利用率の結果を第2表に示す。copper Chebrel phase compound (Cu2MOeS) with an average particle size of 0.8 μm and density = 4.7), e, density = 5.8
) and then a polyethylene solution was added to obtain an electrode powder dispersion (B) with a solid content of 50%. A mixture consisting of CuI and CuC1 at 200
9 obtained by heating reaction in a closed glass container at ℃ for 17 hours Also, copper Chevrel phase compound f;L MO82,
A mixture of Cu and S was heated and reacted in vacuum at 1000°C for 48 hours to obtain a mixture of a predetermined amount of cationic surfactant solution (A), electrode powder dispersion (B), and toluene. Mix and grind in a ball mill for 24 hours to obtain an electrode powder slurry. Apply this slurry on a smooth Teflon plate using a doctor blade in dry nitrogen at 80°C.
After drying, the size is 80x80mm, thickness 154±5
A sheet-like electrode molded body (Bl) with a μm electrode powder content of 85% by volume was obtained, and an electrode molded body (D1) with a thickness of 125±10 μm was obtained.
By mixing gI and WOs in a predetermined ratio and heating and reacting at 400°C in the air for 6 hours, it can be obtained. Q Ags,
yVaOs was obtained by mixing Ag powder and V*Os at a predetermined ratio and heating the mixture in a sealed tube at 550°C for 6 hours (Comparative Example 1). A cationic surfactant was used instead of the solid electrolyte dispersion (B). A sheet-shaped 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 an electrode powder dispersion (C) containing no electrode powder was used (Example 2). A with a silver ion conductive average particle size of 8 μm as
ge I4 WO4 powder, silver vanadate powder (Ags, yVgOs) with an average particle size of 10 μm, and a mixture of Noko:2 were used (\ Electrode powder dispersion (D) containing a cationic surfactant represented by formula (4)) The electrode powder dispersion (E) containing no cationic surfactant was used instead of the electrode powder dispersion (D) in the same manner as in Example 1 except that the electrode powder content was 90% by volume (Comparative Example 2). Example 2 except that
A sheet-like electrode molded body (El) with an electrode powder content of 90% by volume was obtained in the same manner as in (Example 3).
A 1:1 mixture of 1 μm Lil-H20 powder and niobium sulfide powder (NbS*) with an average particle size of 6 μm was used (\
Except for using the electrode powder dispersion (F) containing the cationic surfactant represented by formula (5)! In the same manner as in Example 1, an electrode molded body (Fl) with a thickness of 85 ± 5 μm and an electrode powder content of 90% by volume was obtained.
For bS2, a commercially available reagent was ground in ethyl ether using a ball mill, and for t (Comparative Example 3), instead of the electrode powder dispersion (F), an electrode powder dispersion (G) containing no cationic surfactant was used. Example 3 except that
In Examples 1 to 3 and Comparative Examples 1 to 3, a sheet-like electrode molded body (G1) having an electrode powder content of 90% by volume was obtained in the same manner as above.9 Characteristics of the electrode molded body were evaluated by the method described below. The obtained electrode molded bodies were punched into 20 discs each with a diameter of 10 mm and used as samples for characteristic testing.For the electrode discs of Example 1 and Comparative Example 1, RbCu4I+ and 6C were used as solid electrolytes.
1g of 1s, s powder was molded at a pressure of 200 kg/cm'', and one pellet with a diameter of 10 mm was placed on the top and bottom, and platinum disks were placed above and below the pellets, and the whole was molded with a pressure of 50 kg/cm'' With pressure applied from above and below,
Test battery B was heated at 130°C for 3 hours in a nitrogen gas atmosphere.
Assemble C2 (Example 1) and C2 (Comparative Example 1).
c' for the electrode discs of Example 2 and Comparative Example 2! ,
Similarly, test cells D2 (Example 2) and F2 (Comparative Example 2) were prepared using Age Ia 104 powder as the solid electrolyte.
) Assemble the electrode discs of Example 3 and Comparative Example 3 using LiI/HeO powder as the solid electrolyte, X, test battery F2 using a lithium disc with a thickness of 0.3 m and a diameter of 10 mm as the negative electrode. (Example 3) and G
2 (Comparative Example 3) was assembled (9) F2 and G2 were only pressurized without heating (9) Test batteries B2 and C2, each made up of 10 of the same batteries, were charged at a constant voltage of 0.6 V for 17 hours. almA
Discharge for 10 seconds at a constant current of \ Measure the difference in battery voltage (polarization) immediately before and after discharge, and calculate the average value and standard deviation value for 10 batteries.9 Also, at the same current value up to 0.3V Perform continuous discharge to find the discharge capacity. Find the utilization rate of the electrode active material relative to the theoretical capacity (100%). For test batteries D2 and B2, charge at a constant voltage of 0.50 V for 17 hours at a constant current value of 200 μA and charge ratio of 10 After discharging for seconds, the average value and standard deviation of polarization were determined.Also, continuous discharge was performed at the same current value to 0.3V, and the theoretical capacity (100
9) For test batteries F2 and G2 (1) at a constant current of 50 μA.
Discharge for 0 seconds and find the average value and standard deviation of polarization. 9. Also, at the same current value, 1. Continuously discharge up to Ov and find the utilization rate of the electrode active material with respect to the theoretical capacity (100%).
The results of polarization values are shown in Table 1, and the results of utilization rates are shown in Table 2.
また 電極成形体の曲げ強度を、長さ40mm幅5
mmの成形体を半径が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暇 破断に至るまでの
回数で評価した 結果を第3表に示す。以上の測定値
は何れも20℃での値である。In addition, the bending strength of the electrode molded body was determined by measuring 40 mm in length and 5 mm in width.
Table 3 shows the results of an evaluation based on the number of times a molded product of 50 mm was repeatedly bent at a rate of 2 times per second until breakage occurred along a curved surface with a radius of 50 mm. All of the above measured values are values at 20°C.
実施例1 比較例1 実施例2 比較例2 実施例3 比較例3 第1表 分極 第2表 利用率 * 実施例1 比較例1 実施例2 比較例2 実施例3 比較例3 理論容量を1 第3表 機械強度 電池 機械強度。Example 1 Comparative example 1 Example 2 Comparative example 2 Example 3 Comparative example 3 Table 1 Polarization Table 2 Utilization rate * Example 1 Comparative example 1 Example 2 Comparative example 2 Example 3 Comparative example 3 The theoretical capacity is 1 Table 3 Mechanical strength Battery Mechanical strength.
B2 実施例1145
C2比較例1100
B2 実施例2140
B2 比較例2100
F2 実施例3155
G2 比較例3100
本対応する比較例の曲げ強度を100とした第1表から
第3表に示した結果から明らかなよう凶 本実施例によ
る電極組成物(よ 比較例に較べ電極利用率は高く、分
極の標準偏差値極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4 ま
た 分極の平均値も小さ(t さらに 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らかなよう&ミ 本発明の電極
組成物の製造法によれCTCE○鎖および/またはP○
鎖を含むカチオン界面活性剤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。B2 Example 1145 C2 Comparative Example 1100 B2 Example 2140 B2 Comparative Example 2100 F2 Example 3155 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 100. The electrode composition according to this example has a higher electrode utilization rate than that of the comparative example, and the standard deviation of polarization is small, indicating that it is a homogeneous electrode composition in which the electrode active material and electrolyte are evenly mixed. Waka 4 Also, the average value of polarization is small (t) Furthermore, when comparing the mechanical strength, although the electrode composition of this example has greater strength than the conventional one, it is clear from the description of the example that the effect exceeds the effect of the invention. &mi CTCE○ chain and/or P○
Due to the surfactant action of the cationic surfactant containing chains, it is possible to obtain an electrode slurry that is stable for a long period of time, and by removing the solvent from this slurry and solidifying it, a homogeneous electrode composition can be obtained. This has the effect that a small electrode composition can be obtained.
Claims (1)
び固体電解質粉末を分散して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含む電極組成物の
製造法において、前記スラリー中に、エチレンオキサイ
ド鎖およびプロピレンオキサイド鎖を有するカチオン界
面活性剤、またはエチレンオキサイド鎖、プロピレンオ
キサイド鎖のいづれか一方の界面活剤を添加する電極組
成物の製造法。In the method for producing an electrode composition, the method includes a step of dispersing an electrode active material powder and a solid electrolyte powder to form a slurry in a solvent in which a thermoplastic resin is dissolved, and a step of removing the solvent from the slurry, wherein the slurry contains: A method for producing an electrode composition, in which a cationic surfactant having an ethylene oxide chain and a propylene oxide chain, or a surfactant having either an ethylene oxide chain or a propylene oxide chain is added.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2137812A JPH0433255A (en) | 1990-05-28 | 1990-05-28 | Manufacturing method of electrode composition |
| 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 |
|---|---|---|---|
| JP2137812A JPH0433255A (en) | 1990-05-28 | 1990-05-28 | Manufacturing method of electrode composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0433255A true JPH0433255A (en) | 1992-02-04 |
Family
ID=15207435
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2137812A Pending JPH0433255A (en) | 1990-05-28 | 1990-05-28 | Manufacturing method of electrode composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0433255A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100441513B1 (en) * | 2001-09-05 | 2004-07-23 | 삼성에스디아이 주식회사 | An active material for a battery and a method of preparing the same |
| US11104051B2 (en) | 2018-04-02 | 2021-08-31 | The Japan Steel Works, Ltd. | Molding machine and control method of molding machine |
-
1990
- 1990-05-28 JP JP2137812A patent/JPH0433255A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100441513B1 (en) * | 2001-09-05 | 2004-07-23 | 삼성에스디아이 주식회사 | An active material for a battery and a method of preparing the same |
| US11104051B2 (en) | 2018-04-02 | 2021-08-31 | The Japan Steel Works, Ltd. | Molding machine and control method of molding machine |
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