JPH0594820A - Organic electrolyte battery - Google Patents
Organic electrolyte batteryInfo
- Publication number
- JPH0594820A JPH0594820A JP3253368A JP25336891A JPH0594820A JP H0594820 A JPH0594820 A JP H0594820A JP 3253368 A JP3253368 A JP 3253368A JP 25336891 A JP25336891 A JP 25336891A JP H0594820 A JPH0594820 A JP H0594820A
- Authority
- JP
- Japan
- Prior art keywords
- mixture
- positive electrode
- molding
- electrode mixture
- battery
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
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- Y02E60/12—
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Abstract
(57)【要約】
【目的】 正極合剤の組成および成型密度を適正化する
ことにより、成型正極の機械的強度の上昇による生産性
の向上と、放電特性に優れた、高性能の有機電解質電池
を提供することを目的とする。
【構成】 本発明の有機電解質電池は、活物質としての
二酸化マンガンと、導電剤としてのグラファイトと、結
着剤としてのテトラフルオロエチレン−ヘキサフルオロ
プロピレン共重合体とを主体として混合してなる混合材
料を加圧成型した正極合剤を用い、この正極合剤におけ
る前記グラファイトの配合比率が0.5〜25重量%、
前記テトラフルオロエチレン−ヘキサフルオロプロピレ
ン共重合体の配合比率が0.5〜5重量%であり、また
前記正極合剤の成型密度を前記混合材料の嵩密度の2.
4〜3倍としたものである。
(57) [Summary] [Purpose] A high-performance organic electrolyte with improved discharge characteristics and improved productivity by increasing the mechanical strength of the molded positive electrode by optimizing the composition and molding density of the positive electrode mixture. The purpose is to provide a battery. The organic electrolyte battery of the present invention is a mixture mainly composed of manganese dioxide as an active material, graphite as a conductive agent, and tetrafluoroethylene-hexafluoropropylene copolymer as a binder. Using a positive electrode mixture obtained by pressure molding a material, the compounding ratio of the graphite in the positive electrode mixture is 0.5 to 25% by weight,
The compounding ratio of the tetrafluoroethylene-hexafluoropropylene copolymer is 0.5 to 5% by weight, and the molding density of the positive electrode mixture is the bulk density of the mixed material of 2.
4 to 3 times.
Description
【0001】[0001]
【産業上の利用分野】本発明は、有機電解質電池に関
し、特にリチウム,ナトリウムなどの軽金属を負極活物
質とし、二酸化マンガン,ふっ化黒鉛などを正極活物質
とし、電解質として過塩素酸リチウム,硼ふっ化リチウ
ムなどを溶解させたプロピレンカーボネート,ジメトキ
シエタン,γ−ブチロラクトンなどの単体もしくは、混
合溶液を電解液として用いた正極を改良した有機電解質
リチウム電池に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an organic electrolyte battery, and in particular, a light metal such as lithium and sodium as a negative electrode active material, manganese dioxide, graphite fluoride and the like as a positive electrode active material, and lithium perchlorate and boron as electrolytes. The present invention relates to an organic electrolyte lithium battery in which a positive electrode is improved by using a simple substance or a mixed solution of propylene carbonate, dimethoxyethane, γ-butyrolactone and the like in which lithium fluoride or the like is dissolved, as an electrolytic solution.
【0002】[0002]
【従来の技術】インサイドアウト形やコイン形などのリ
チウム電池では、活物質である二酸化マンガンに、導電
剤としてグラファイト、また結着剤としてポリテトラフ
ルオロエチレンをそれぞれ混合し、ついでこれらの混合
粉末(以下、混合した正極材料の粉末を合剤と称する)
を高圧で加圧成型した正極合剤が用いられている。この
ように加圧成型した正極合剤として、従来は活物質,導
電剤および結着剤などの混合材料の嵩密度の2倍程度の
成型密度のものが用いられている。2. Description of the Related Art In lithium batteries such as inside-out type and coin type, manganese dioxide, which is an active material, is mixed with graphite as a conductive agent and polytetrafluoroethylene as a binder, and then mixed powder ( Hereinafter, the mixed positive electrode material powder is referred to as a mixture)
A positive electrode mixture obtained by pressure-molding is used. As the positive electrode mixture thus pressure-molded, conventionally, a mixture having a molding density of about twice the bulk density of a mixed material such as an active material, a conductive agent and a binder has been used.
【0003】つまり、従来は電解液が多いほど電池の放
電特性が良いとの観点から、電池の組み立て工程上、支
障がない強度を保つ範囲で正極合剤の成型を緩く行い、
正極合剤の成型密度を低くし、正極合剤における吸液性
を高めて電解液を多量に吸液させるようにしている。ま
た、正極合剤には成型を容易にするために結着剤を使用
している。That is, conventionally, from the viewpoint that the more the amount of the electrolytic solution is, the better the discharge characteristics of the battery are, the positive electrode mixture is loosely molded within a range in which the strength does not hinder the assembly process of the battery.
The molding density of the positive electrode mixture is lowered, and the liquid absorbing property of the positive electrode mixture is improved to absorb a large amount of the electrolytic solution. Further, a binder is used for the positive electrode mixture in order to facilitate molding.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、このよ
うに成型密度の低い正極合剤を用いた場合、放電途中に
おける正極合剤の膨潤が著しく、電解液を必要以上に吸
収する。このため、放電進行とともに電解液が枯渇し、
電池の内部抵抗が増大して放電特性の急激な低下が起こ
るという問題がある。However, when such a positive electrode mixture having a low molding density is used, the positive electrode mixture swells remarkably during discharge and absorbs the electrolytic solution more than necessary. Therefore, the electrolyte is depleted as the discharge progresses,
There is a problem in that the internal resistance of the battery increases and the discharge characteristics suddenly deteriorate.
【0005】また、正極合剤組成中に結着剤としてテト
ラフルオロエチレンの重合体を使用する場合、正極合剤
の成型密度を一定以上にすることが難しく成型強度が不
足し、正極合剤の取り扱いが難しいという問題点があ
る。さらにテトラフルオロエチレンの性質から正極合剤
の比抵抗を上昇させやすく、電池特性の低下を起こしや
すいという問題がある。Further, when a polymer of tetrafluoroethylene is used as a binder in the composition of the positive electrode mixture, it is difficult to keep the molding density of the positive electrode mixture above a certain level, and the molding strength is insufficient. There is a problem that it is difficult to handle. Further, due to the property of tetrafluoroethylene, there is a problem that the specific resistance of the positive electrode mixture is easily increased and the battery characteristics are likely to be deteriorated.
【0006】本発明はこのような課題を解決するもの
で、正極合剤の組成および成型密度を適正化し、放電性
能の改良と正極合剤の生産性を向上した有機電解質電池
を提供することを目的とする。The present invention is intended to solve such problems, and to provide an organic electrolyte battery in which the composition and molding density of the positive electrode mixture are optimized to improve the discharge performance and the productivity of the positive electrode mixture. To aim.
【0007】[0007]
【課題を解決するための手段】この課題を解決するため
本発明の有機電解質電池は、活物質としての二酸化マン
ガンと、導電剤としてのグラファイトと、結着剤として
のテトラフルオロエチレン−ヘキサフルオロプロピレン
共重合体とを主体として混合してなる混合材料を加圧成
型した正極合剤を備え、この正極合剤における前記グラ
ファイトの配合比率が0.5〜25重量%、前記テトラ
フルオロエチレン−ヘキサフルオロプロピレン共重合体
の配合比率が0.5〜5重量%であり、また前記正極合
剤の成型密度を前記活物質,導電剤および結着剤を主体
とする混合材料の嵩密度の2.4%〜3倍としたもので
ある。In order to solve this problem, the organic electrolyte battery of the present invention comprises manganese dioxide as an active material, graphite as a conductive agent, and tetrafluoroethylene-hexafluoropropylene as a binder. A positive electrode mixture obtained by pressure-molding a mixed material mainly composed of a copolymer is provided, and the compounding ratio of the graphite in the positive electrode mixture is 0.5 to 25% by weight, and the tetrafluoroethylene-hexafluoro The compounding ratio of the propylene copolymer is 0.5 to 5% by weight, and the molding density of the positive electrode mixture is 2.4 of the bulk density of the mixed material mainly containing the active material, the conductive agent and the binder. % To 3 times.
【0008】[0008]
【作用】この構成により本発明の有機電解質電池は、正
極合剤の成型密度を上記の範囲に規定することで、放電
進行時における正極合剤の膨潤が有効に押さえられ、そ
の結果、正極合剤による電解液の吸収が抑制され、正極
合剤と負極リチウムの間の電解液の枯渇が防止される。
この結果、放電に伴う電池の内部抵抗の上昇が抑制さ
れ、電池の放電性能が向上する。With this configuration, in the organic electrolyte battery of the present invention, by regulating the molding density of the positive electrode mixture within the above range, the swelling of the positive electrode mixture during the progress of discharge is effectively suppressed, and as a result, the positive electrode mixture is The absorption of the electrolytic solution by the agent is suppressed, and the exhaustion of the electrolytic solution between the positive electrode mixture and the negative electrode lithium is prevented.
As a result, the increase in internal resistance of the battery due to discharge is suppressed, and the discharge performance of the battery is improved.
【0009】また、正極合剤内のグラファイト、および
結着剤の配合比率の適正化により、正極合剤の導電性が
良くなり、電池の放電性能および生産性が向上する。さ
らに、正極合剤のグラファイト比率、および結着剤の配
合比率を上記の範囲に規定することで正極合剤の成型を
容易にすることができると同時に、正極合剤の機械的強
度をアップでき、生産性を上げることができる。Further, by optimizing the blending ratio of graphite and the binder in the positive electrode mixture, the conductivity of the positive electrode mixture is improved, and the discharge performance and productivity of the battery are improved. Further, by defining the graphite ratio of the positive electrode mixture and the compounding ratio of the binder within the above ranges, molding of the positive electrode mixture can be facilitated, and at the same time, the mechanical strength of the positive electrode mixture can be increased. , Can increase productivity.
【0010】[0010]
【実施例】正極合剤の成型密度を従来値より大きくした
場合、放電途中の合成膨張による放電性能の低下が抑制
でき、電池の放電性能の向上が図れることがわかった。
また、正極合剤の結着剤としてポリテトラフルオロエチ
レンの代わりにテトラフルオロエチレン−ヘキサフルオ
ロプロピレン共重合体を用いた場合、ポリテトラフルオ
ロエチレンを使用した場合に比べて、正極の成型密度を
より大きくすることができ、正極合剤の成型強度をアッ
プすることができる。本発明の組成の正極合剤を使用し
て正極合剤を成型した場合、正極合剤の成型密度/混合
材料の嵩密度の値が2〜3倍の範囲にあることも見いだ
した。さらに、テトラフルオロエチレン−ヘキサフルオ
ロプロピレン共重合体を結着剤とした場合、正極合剤の
比抵抗も低く維持でき、結着剤を使用することによる電
池の内部抵抗の上昇を押さえることができ、放電性能の
低下を防ぐことができることも明らかになった。本発明
はこのような知見に基づくものであり、正極活物質とし
ての二酸化マンガンと、導電剤としてのグラファイト
と、結着剤としてのテトラフルオロエチレン−ヘキサフ
ルオロプロピレン共重合体とを主体として混合してなる
合剤を加圧成型した正極合剤を用い、この正極合剤にお
けるグラファイトの配合比率が、0.5〜25重量%、
テトラフルオロエチレン−ヘキサフルオロプロピレン共
重合体の配合比率が、0.5〜5重量%であり、また、
この正極合剤の成型密度g/cm3を正極合剤の混合材料
の嵩密度g/cm3(以下、成型密度/嵩密度と略す)の
2.4〜3倍程度としたことを主旨とするインサイドア
ウト構造を持つ円筒形リチウム電池である。なお、成型
密度/嵩密度が2倍程度というのは、本発明の正極合剤
配合比率の範囲では、二酸化マンガンの配合比率を多く
して、グラファイト、および結着剤の配合比率を低くす
るか、または成型時の加圧力を加減させることによって
可能である。[Examples] It has been found that when the molding density of the positive electrode mixture is made higher than the conventional value, the deterioration of the discharge performance due to the synthetic expansion during the discharge can be suppressed, and the discharge performance of the battery can be improved.
Further, when tetrafluoroethylene-hexafluoropropylene copolymer was used instead of polytetrafluoroethylene as the binder of the positive electrode mixture, the molding density of the positive electrode was better than that when polytetrafluoroethylene was used. It can be increased, and the molding strength of the positive electrode mixture can be increased. It has also been found that when the positive electrode mixture is molded using the positive electrode mixture having the composition of the present invention, the value of the molding density of the positive electrode mixture / the bulk density of the mixed material is in the range of 2 to 3 times. Furthermore, when tetrafluoroethylene-hexafluoropropylene copolymer is used as a binder, the specific resistance of the positive electrode mixture can be kept low, and the increase in internal resistance of the battery due to the use of the binder can be suppressed. It was also clarified that the deterioration of discharge performance can be prevented. The present invention is based on such knowledge, and is mainly mixed with manganese dioxide as a positive electrode active material, graphite as a conductive agent, and tetrafluoroethylene-hexafluoropropylene copolymer as a binder. Using a positive electrode mixture obtained by pressure-molding the mixture, the graphite content in the positive electrode mixture is 0.5 to 25 wt%,
The compounding ratio of the tetrafluoroethylene-hexafluoropropylene copolymer is 0.5 to 5% by weight, and
The purpose is to set the molding density g / cm 3 of the positive electrode mixture to about 2.4 to 3 times the bulk density g / cm 3 of the mixed material of the positive electrode mixture (hereinafter, abbreviated as molding density / bulk density). It is a cylindrical lithium battery with an inside-out structure that In addition, the molding density / bulk density is about 2 times means that the compounding ratio of manganese dioxide should be increased and the compounding ratio of graphite and the binder should be lowered within the range of the compounding ratio of the positive electrode mixture of the present invention. Alternatively, it is possible to adjust the pressure applied during molding.
【0011】しかしながら、正極合剤中のグラファイト
の配合比を低下させて成型密度をアップさせる場合に
は、正極合剤に盛りこまれる活物質の理論容量は上昇す
るものの、グラファイトの配合比率の減少により正極合
剤の導電性が低下し、電池の放電反応時において正極合
剤中の活物質の反応が不均一になりやすく、その結果反
応合剤の比抵抗が上昇し、放電中の電池電圧をばらつか
せる原因となる。一方、成型密度/嵩密度を3倍程度に
するには、正極活物質の二酸化マンガンの配合比率を減
少させ、グラファイトの配合比率を増加させた場合には
(配合比率が23%以上)正極合剤の導電性は上昇する
(比抵抗は減少する)が、正極合剤内の活物質量の絶対
量が減り、電池の放電性能を低下させる。さらに、正極
合剤内のグラファイトの比率が増加する結果、合剤を加
圧成型する際、成型性がアップする。そのため、電池を
構成した後、正極合剤に電解液がほとんど吸収されなく
なる。その結果放電反応時に、正極合剤内の電解液は不
均一になりやすくなり、放電中の電池電圧をばらつかせ
る原因となり、電池性能低下の一因となる。However, when the compounding ratio of graphite in the positive electrode mixture is decreased to increase the molding density, the theoretical capacity of the active material contained in the positive electrode mixture increases, but the compounding ratio of graphite decreases. As a result, the conductivity of the positive electrode mixture decreases, and the reaction of the active material in the positive electrode mixture tends to become non-uniform during the discharge reaction of the battery, resulting in an increase in the specific resistance of the reaction mixture and the battery voltage during discharge. It causes to disperse. On the other hand, in order to triple the molding density / bulk density, the compounding ratio of manganese dioxide in the positive electrode active material should be decreased, and the compounding ratio of graphite should be increased (the compounding ratio is 23% or more). Although the conductivity of the agent increases (the specific resistance decreases), the absolute amount of the active material in the positive electrode mixture decreases, which deteriorates the discharge performance of the battery. Further, as a result of the increase in the ratio of graphite in the positive electrode mixture, the moldability is improved when the mixture is pressure-molded. Therefore, the electrolyte solution is hardly absorbed by the positive electrode mixture after the battery is constructed. As a result, during the discharge reaction, the electrolyte solution in the positive electrode mixture is likely to become non-uniform, which causes variations in the battery voltage during discharge, which is a cause of battery performance degradation.
【0012】以下に、添付の図面を用いて本発明の一実
施例の有機電解質電池について説明する。An organic electrolyte battery according to an embodiment of the present invention will be described below with reference to the accompanying drawings.
【0013】二酸化マンガン(MnO2)とグラファイ
ト(Gr)、ならびにテトラフルオロエチレン−ヘキサ
フルオロプロピレン共重合体を(表1)に示す配合比
(重量%)にて、混合してなる合剤A1および、本実施
例に対する比較例として、二酸化マンガンとグラファイ
トならびにテトラフルオロエチレン(TFE単体)を
(表2)に示す配合比(重量%)にて混合してなる合剤
A2をそれぞれ図1(a)に示すように、円板状合剤成
型用上金型1と、円板状合剤成型用下金型2により加圧
圧縮して、円板状合剤3を成型した。そして、この円板
状合剤3を粉砕し、さらにふるいにかけて、それぞれ
(表1)と(表2)に示す14〜50メッシュの粒径の
造粒合剤A1(1)〜(12),A2(1)〜(12)を得
た。なお、これらの造粒合剤A1(1)〜(12)、A2
(1)〜(12)の嵩密度および各造粒合剤の比抵抗を
(表1),(表2)にあわせて示した。Manganese dioxide (MnO 2 ) and graphite (Gr), and tetrafluoroethylene-hexafluoropropylene copolymer were mixed at the compounding ratio (% by weight) shown in (Table 1) to prepare mixture A1 and As a comparative example to this example, a mixture A2 prepared by mixing manganese dioxide, graphite, and tetrafluoroethylene (TFE alone) at a compounding ratio (wt%) shown in (Table 2) is shown in FIG. 1 (a). As shown in FIG. 3, the disc-shaped mixture mixture 3 was molded by pressurizing and compressing with the disc-shaped mixture mixture upper die 1 and the disc-shaped mixture mixture lower die 2. Then, the disc-shaped mixture 3 was pulverized and further sifted, and the granulated mixture A1 (1) to (12) having a particle size of 14 to 50 mesh shown in (Table 1) and (Table 2), respectively, A2 (1) to (12) were obtained. In addition, these granulation mixtures A1 (1) to (12), A2
The bulk densities of (1) to (12) and the specific resistance of each granulation mixture are also shown in (Table 1) and (Table 2).
【0014】[0014]
【表1】 [Table 1]
【0015】[0015]
【表2】 [Table 2]
【0016】造粒合剤の比抵抗は断面積1cm2の型に1.
5gの造粒合剤をはさみ、200kg/cm2の加圧をか
けた時の造粒合剤の抵抗を測定し、造粒合剤の比抵抗を
求めたものである。(表1)から明らかなようにA1
(1)〜(12)の造粒合剤の方がA2(1)〜(12)の
造粒合剤のいずれに対しても嵩密度は高く、比抵抗は低
い。このことは、電池とする場合A1(1)〜(12)の
造粒合剤を使用すれば、正極の合剤密度を一定以上にし
やすく、かつ放電時における電池内の正極に係わる抵抗
成分をA2(1)〜(12)の造粒合剤使用時に比べ低下
させることができ放電,特性向上に有効であることを示
す。合剤比抵抗が低下する理由としては、本実施例のA
1(1)〜(12)の造粒合剤に使用する結着剤のテトラ
フルオロエチレン−ヘキサフルオロプロピレン共重合体
は合剤中で粒状の形状となり、合剤間に入りこみ合剤粒
子同志を接合すると考えられるに対し、テトラフルオロ
エチレンを結着剤とした場合に、テトラフルオロエチレ
ンは合剤内で繊維状、もしくは板状となり合剤粒子にか
らんで、合剤粒子を接合するため合剤粒子の間隔が開く
ためと考えられる。この結果、合剤成型時に合剤粒子間
にすきまが生じやすくなり、結果として合剤嵩比重の低
下の原因となり、一方、電解液を合剤粒子間に取りこみ
やすいため電池を構成した場合、反応上イオン移動に必
要な電解液が不足しやすいと考えられる。The specific resistance of the granulated mixture is 1 the type of cross-sectional area 1 cm 2.
The specific resistance of the granulation mixture was determined by sandwiching 5 g of the granulation mixture and measuring the resistance of the granulation mixture when applying a pressure of 200 kg / cm 2 . As is clear from (Table 1), A1
The granule mixture of (1) to (12) has a higher bulk density and lower specific resistance than any of the granule mixtures of A2 (1) to (12). This means that if the granulated mixture of A1 (1) to (12) is used in the case of a battery, the mixture density of the positive electrode can be easily kept above a certain level, and the resistance component related to the positive electrode in the battery during discharge can be A2 (1) to (12) shows that it can be lowered compared to when using the granulation mixture and is effective in improving discharge and characteristics. The reason why the resistivity of the mixture is lowered is that
The binder tetrafluoroethylene-hexafluoropropylene copolymer used in 1 (1) to (12) for the granulation mixture has a granular shape in the mixture and enters between the mixture to form a mixture of the mixture particles. While it is considered that the particles are joined, when tetrafluoroethylene is used as a binder, the tetrafluoroethylene becomes fibrous or plate-like inside the mixture and is entangled with the mixture particles to bond the mixture particles. It is thought that this is due to the spacing between particles. As a result, a gap is liable to be generated between the mixture particles during the mixture molding, resulting in a decrease in the mixture bulk specific gravity. On the other hand, when the battery is configured because the electrolyte is easily incorporated between the mixture particles, the reaction It is considered that the electrolyte solution required for upper ion transfer is likely to run short.
【0017】次に、図1(d)に示したように、これら
の造粒合剤A1,A2をそれぞれ中空円筒状合剤成型用
下金型4の凹部(i)に盛り込み、また下記の方法で造
粒合剤の盛り込み量を調整した。そして、中空円筒状合
剤成型用下金型4の上面4aから、中空円筒状合剤成型
用下金型4に対応する形状の図1(e)に示す中空円筒
状合剤成型用上金型(パンチ)5で加圧することによ
り、これら造粒合剤A1(1)〜(12),A2(1)〜
(12)を、図1(f)のように、外径15mm、内径11
mm、高さ14mmの中空円筒状正極合剤6を加圧成型し
た。この時、図1(f)に示す中空円筒状正極合剤6の
圧縮面イにパンチ5があたるように加圧する。また、圧
縮面イにおける成型圧を3ton/cm2になるようにし
た。そして、このようにして中空円筒状正極合剤(以
下、正極合剤と略す)6の成型を行い、また成型密度/
嵩密度の比を2.1〜3.2程度の範囲で変化させた正極
合剤を種々作り評価した。成型した正極合剤の組成によ
る成型性の差の評価は、次の方法を用いた。すなわち、
成型合剤6の中心軸に対して垂直方向から荷重をかけ、
成型合剤6が破壊するまでの荷重値により成型合剤6の
成型時の強度を定義し、その破壊時の荷重値の差を求め
た。この場合、成型合剤6を加圧成型する際の圧力、お
よび成型合剤6の重量が一定なので、成型合剤6の破壊
時の荷重値の差は、合剤組成の違いによるものと考えら
れる。また、これらの成型合剤6をそれぞれ用い、図2
に示した構造のインサイドアウト構造のリチウム電池を
それぞれ5個ずつ作製した。図2において、11は負極
端子を兼ねる負極キャップ、12は安全弁、13は封口
板構成部材、14はガスケット、15は正極端子を兼ね
る正極ケース、16は成型された正極合剤、17は負極
リード、18は負極リチウムにつけられた集電体、19
は筒状に形成した負極リチウム、20は負極リチウム1
9をくるむように筒状に成型されたセパレータ、21は
塩化ビニール製(PVC)外装チューブである。Next, as shown in FIG. 1 (d), each of these granulation mixes A1 and A2 is placed in the recess (i) of the hollow cylindrical mixture molding lower die 4 and the The amount of the granulated mixture incorporated was adjusted by the method. Then, from the upper surface 4a of the hollow cylindrical mixture molding lower die 4, a hollow cylindrical mixture molding upper die shown in FIG. 1 (e) having a shape corresponding to the hollow cylindrical mixture molding lower die 4 is formed. By pressurizing with a mold (punch) 5, these granulation mixtures A1 (1) to (12), A2 (1) to
As shown in Fig. 1 (f), (12) has an outer diameter of 15 mm and an inner diameter of 11
A hollow cylindrical positive electrode mixture 6 having a height of 14 mm and a height of 14 mm was pressure-molded. At this time, pressure is applied so that the punch 5 hits the compression surface B of the hollow cylindrical positive electrode mixture 6 shown in FIG. Further, the molding pressure on the compression surface B was set to 3 ton / cm 2 . In this way, the hollow cylindrical positive electrode mixture (hereinafter abbreviated as positive electrode mixture) 6 is molded, and the molding density /
Various positive electrode mixtures having different bulk density ratios in the range of about 2.1 to 3.2 were prepared and evaluated. The following method was used to evaluate the difference in moldability depending on the composition of the molded positive electrode mixture. That is,
A load is applied from the direction perpendicular to the central axis of the molding mixture 6,
The strength of the molding mixture 6 at the time of molding was defined by the load value until the molding mixture 6 was broken, and the difference between the load values at the time of breaking was determined. In this case, since the pressure when the molding mixture 6 is pressure-molded and the weight of the molding mixture 6 are constant, it is considered that the difference in the load value when the molding mixture 6 is broken is due to the difference in the composition of the mixture. Be done. In addition, each of these molding mixtures 6 was used, and FIG.
Five lithium batteries each having an inside-out structure having the structure shown in were prepared. In FIG. 2, 11 is a negative electrode cap also serving as a negative electrode terminal, 12 is a safety valve, 13 is a sealing plate constituent member, 14 is a gasket, 15 is a positive electrode case also serving as a positive electrode terminal, 16 is a molded positive electrode mixture, and 17 is a negative electrode lead. , 18 is a current collector attached to the negative electrode lithium, 19
Is a negative electrode lithium formed in a cylindrical shape, 20 is a negative electrode lithium 1
A separator formed in a tubular shape so as to wrap 9 and a vinyl chloride (PVC) outer tube 21.
【0018】これらの成型合剤A1(1)〜(12),A
2(1)〜(12)における成型密度/嵩密度の比、並び
に成型合剤への荷重による合剤破壊時の荷重値を(表
3),(表4)に示した。These molding mixtures A1 (1) to (12), A
2 (1) to (12), the ratio of the molding density / bulk density, and the load values when the mixture is broken by the load on the molding mixture are shown in (Table 3) and (Table 4).
【0019】[0019]
【表3】 [Table 3]
【0020】[0020]
【表4】 [Table 4]
【0021】また、これらの成型合剤A1(1)〜(1
2),A2(1)〜(12)をそれぞれ用いて電池5個ず
つ作り、これらおのおのについて温度20℃において放
電抵抗2.7kΩで終止電圧2.0Vまで連続放電させて
それらの放電持続時間を調べた。結果は(表5)の通り
である(それぞれ5個の電池の放電時間の平均値)。Further, these molding mixtures A1 (1) to (1
2), A5 (1) to (12) are used to make 5 batteries each, and each of them is continuously discharged to a final voltage of 2.0V with a discharge resistance of 2.7kΩ at a temperature of 20 ° C, and their discharge duration is Examined. The results are shown in (Table 5) (average value of discharge time of 5 batteries each).
【0022】[0022]
【表5】 [Table 5]
【0023】一方、上記の圧縮面における成型圧力を5
ton,および2ton/cm2とした他は同様にしてイ
ンサイドアウト型リチウム電池を種々作り、これらの電
池を同じ条件で連続放電させてそれぞれ放電持続時間を
調べた(試験結果は表5に示してある)。On the other hand, the molding pressure on the compression surface is 5
Various inside-out type lithium batteries were made in the same manner except that they were set to ton and 2 ton / cm 2, and these batteries were continuously discharged under the same conditions and their discharge durations were examined (test results are shown in Table 5). is there).
【0024】以上の実験結果を前記成型圧毎に、縦軸に
放電持続時間を、横軸には成型密度/嵩密度の比を採っ
てプロットしたところ、図3に示したグラフ(グラフに
は2tonと3tonで成型した成型合剤A1,A2の
結着剤の配合比1%の場合のデータを示してある)を得
た。図3より、成型密度/嵩密度の比を約2.4倍以上
とすれば、本実施例による正極合剤使用の電池は、従来
例で述べた比較組成の正極合剤使用の電池よりも、良好
な放電性能が得られることがわかる。この結果より、成
型面における成型圧を3ton/cm2以上とし、さらに
成型合剤の成型密度/嵩密度の値が、2.4〜3.0程度
とした場合には良好な放電性能が得られ、成型後の合剤
の強度が優れることがわかる。The above experimental results were plotted for each molding pressure by plotting the discharge duration on the vertical axis and the ratio of molding density / bulk density on the horizontal axis. The graph shown in FIG. 2 ton and 3 ton of the molding mixture A1 and A2, the data for the case where the compounding ratio of the binder is 1% is obtained). From FIG. 3, if the ratio of molding density / bulk density is about 2.4 times or more, the battery using the positive electrode mixture according to this example is more than the battery using the positive electrode mixture of the comparative composition described in the conventional example. It can be seen that good discharge performance can be obtained. From these results, good discharge performance was obtained when the molding pressure on the molding surface was 3 ton / cm 2 or more and the molding density / bulk density value of the molding mixture was about 2.4 to 3.0. It can be seen that the strength of the mixture after molding is excellent.
【0025】ところで、図3のグラフの各測定点の合剤
配合比は異なっている。つまり、成型密度/嵩密度の比
が小さいほど、導電剤(この場合はグラファイト)が少
なくなり、一方、成型する場合、一定寸法の成型合剤を
得るために、成型機の成型金型への造粒合剤投入量、つ
まり、盛り込み量を加減し、3tonの加圧力の時、一
定寸法の成型合剤が得られるようにする(これは、成型
機により調整が可能である)。そして、嵩密度が大きい
もの、すなわち、グラファイトが少ないものは、盛り込
み量(体積)が少なく、また、圧縮比(盛り込み体積/
成型合剤体積)は小さい。逆にグラファイトが多い場
合、圧縮比は大きくなる。結果として、グラファイト量
の増加による成型密度の減少よりも嵩密度の減少のほう
が大きいために、成型密度/嵩密度の比は大きくなる。By the way, the mixture mixture ratio at each measurement point in the graph of FIG. 3 is different. In other words, the smaller the molding density / bulk density ratio, the less conductive agent (graphite in this case). On the other hand, when molding, in order to obtain a molding mixture of a certain size The amount of the granulated mixture added, that is, the amount of the granulated mixture, is adjusted so that a molding mixture having a constant size can be obtained at a pressure of 3 tons (this can be adjusted by a molding machine). In addition, a material having a large bulk density, that is, a material having a small amount of graphite has a small amount (volume) of incorporation and a compression ratio (volume of incorporation / volume).
Molding mixture volume) is small. On the contrary, when the amount of graphite is large, the compression ratio becomes large. As a result, the ratio of the molding density / bulk density becomes large because the decrease in the bulk density is larger than the decrease in the molding density due to the increase in the amount of graphite.
【0026】この際、成型合剤の重量は、各点で異な
り、正極理論容量はグラファイト量が多くなるほど減少
するが、その分、合剤の導電性は向上するため、電池性
能としては良くなる。また、以上は円筒状リチウム電池
についての例であるが、その他、例えば本発明をコイン
形、もしくはボタン形リチウム電池に適用し、この電池
に用いる円盤状の正極合剤を同様にして加圧成型した場
合にも、同様な結果が得られることは明らかである。な
お、以上は造粒合剤を加圧成型して作った正極合剤を用
いた例であるが、この他、混合合剤を造粒することなく
秤量し、また加圧成型して作製した正極合剤を用いた場
合にも同様な結果が得られた。At this time, the weight of the molding mixture is different at each point, and the theoretical capacity of the positive electrode decreases as the amount of graphite increases, but the conductivity of the mixture is improved by that much, resulting in better battery performance. .. Further, the above is an example of a cylindrical lithium battery, but in addition, for example, the present invention is applied to a coin-shaped or button-shaped lithium battery, and a disk-shaped positive electrode mixture used in this battery is similarly pressure-molded. It is clear that the same result can be obtained when the above is done. The above is an example of using a positive electrode mixture prepared by pressure molding a granulated mixture, but in addition to this, a mixed mixture was weighed without granulation and prepared by pressure molding. Similar results were obtained when the positive electrode mixture was used.
【0027】[0027]
【発明の効果】以上の実施例の説明により明らかなよう
に、本発明の有機電解質電池によれば、放電進行時にお
ける正極合剤の膨潤が有効に押さえられ、このため放電
に伴う内部抵抗の上昇が抑制されて電池の放電性能向上
が図れると同時に、合剤成型時の強度が十分に得られる
といった効果を奏する。よって工業的利用価値は大なる
ものである。As is clear from the above description of the embodiments, according to the organic electrolyte battery of the present invention, the swelling of the positive electrode mixture during the progress of discharge is effectively suppressed, and therefore the internal resistance due to discharge is increased. It is possible to suppress the rise and improve the discharge performance of the battery, and at the same time, it is possible to obtain sufficient strength at the time of molding the mixture. Therefore, the industrial utility value is great.
【図1】(a)本発明の一実施例における有機電解質電
池の正極合剤製造用に用いる造粒合剤の製造用に用いる
円板状合剤成型用上金型の斜視図 (b)同下金型の斜視図 (c)同円板状合剤の斜視図 (d)同中空円筒状正極合剤の製造用に用いる成型用下
金型の斜視図 (e)同上金型の斜視図 (f)同中空円筒状正極合剤の斜視図FIG. 1 (a) is a perspective view of an upper mold for molding a disc-shaped mixture used for producing a granulated mixture used for producing a positive electrode mixture of an organic electrolyte battery in one example of the present invention (b). A perspective view of the lower mold (c) A perspective view of the same disk-shaped mixture (d) A perspective view of a lower mold for molding used for manufacturing the same hollow cylindrical positive electrode mixture (e) A perspective view of the same mold Figure (f) Perspective view of the same hollow cylindrical positive electrode mixture
【図2】同インサイドアウト構造のリチウム電池の縦断
面図FIG. 2 is a vertical sectional view of the lithium battery having the same inside-out structure.
【図3】本発明の一実施例および比較例の有機電解質電
池の放電特性を示したグラフFIG. 3 is a graph showing discharge characteristics of organic electrolyte batteries of one example and a comparative example of the present invention.
【符号の説明】 1 円板状合剤成型用上金型 2 円板状合剤成型用下金型 3 円板状合剤 4 中空円筒状合剤成型用下金型 5 中空円筒状合剤成型用上金型(パンチ) 6 中空円筒状合剤[Explanation of reference numerals] 1 upper mold for molding disc-shaped mixture 2 lower mold for molding disc-shaped mixture 3 disc-shaped mixture 4 lower mold for molding hollow cylindrical mixture 5 hollow cylindrical mixture Upper mold (punch) for molding 6 Hollow cylindrical mixture
フロントページの続き (72)発明者 寺尾 佳樹 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 ▲よし▼田 正彦 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 横山 敬士 大阪府門真市大字門真1006番地 松下電器 産業株式会社内Front page continuation (72) Inventor Yoshiki Terao, 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. 72) Inventor Keishi Yokoyama 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.
Claims (1)
剤としてのグラファイトと、結着剤としてのテトラフル
オロエチレン−ヘキサフルオロプロピレン共重合体とを
主体として混合してなる混合材料を加圧成型した正極合
剤を備え、この正極合剤における前記グラファイトの配
合比率が0.5〜25重量%、前記テトラフルオロエチ
レン−ヘキサフルオロプロピレン共重合体の配合比率が
0.5〜5重量%であり、また前記正極合剤の成型密度
を前記活物質,導電剤および結着剤を主体とする混合材
料の嵩密度の2.4%〜3倍とした有機電解質電池。1. A mixed material obtained by mainly mixing manganese dioxide as an active material, graphite as a conductive agent, and tetrafluoroethylene-hexafluoropropylene copolymer as a binder, was press-molded. A positive electrode mixture, wherein the graphite has a blending ratio of 0.5 to 25% by weight, and the tetrafluoroethylene-hexafluoropropylene copolymer has a blending ratio of 0.5 to 5% by weight; An organic electrolyte battery in which the molding density of the positive electrode mixture is 2.4% to 3 times the bulk density of the mixed material mainly containing the active material, the conductive agent and the binder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3253368A JPH0594820A (en) | 1991-10-01 | 1991-10-01 | Organic electrolyte battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3253368A JPH0594820A (en) | 1991-10-01 | 1991-10-01 | Organic electrolyte battery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0594820A true JPH0594820A (en) | 1993-04-16 |
Family
ID=17250381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3253368A Pending JPH0594820A (en) | 1991-10-01 | 1991-10-01 | Organic electrolyte battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0594820A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07284781A (en) * | 1994-04-15 | 1995-10-31 | Matsushita Electric Works Ltd | Calcium formulation for ionic water producing device |
| JP2023547117A (en) * | 2020-10-21 | 2023-11-09 | エルジー エナジー ソリューション リミテッド | Electrode powder for producing a dry electrode for secondary batteries, a method for producing the same, a method for producing a dry electrode using the same, a dry electrode, a secondary battery including the same, an energy storage device, and an apparatus for producing a dry electrode |
-
1991
- 1991-10-01 JP JP3253368A patent/JPH0594820A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07284781A (en) * | 1994-04-15 | 1995-10-31 | Matsushita Electric Works Ltd | Calcium formulation for ionic water producing device |
| JP2023547117A (en) * | 2020-10-21 | 2023-11-09 | エルジー エナジー ソリューション リミテッド | Electrode powder for producing a dry electrode for secondary batteries, a method for producing the same, a method for producing a dry electrode using the same, a dry electrode, a secondary battery including the same, an energy storage device, and an apparatus for producing a dry electrode |
| US12586773B2 (en) | 2020-10-21 | 2026-03-24 | Lg Energy Solution, Ltd. | Powder for electrode for manufacturing dry electrode for secondary battery, method for preparing the same, method for manufacturing dry electrode using the same, dry electrode, secondary battery including the same, energy storage apparatus |
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