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JPH0410713B2 - - Google Patents
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JPH0410713B2 - - Google Patents

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Publication number
JPH0410713B2
JPH0410713B2 JP57026354A JP2635482A JPH0410713B2 JP H0410713 B2 JPH0410713 B2 JP H0410713B2 JP 57026354 A JP57026354 A JP 57026354A JP 2635482 A JP2635482 A JP 2635482A JP H0410713 B2 JPH0410713 B2 JP H0410713B2
Authority
JP
Japan
Prior art keywords
current
positive electrode
internal resistance
organic electrolyte
active material
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
Application number
JP57026354A
Other languages
Japanese (ja)
Other versions
JPS58142767A (en
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 filed Critical
Priority to JP57026354A priority Critical patent/JPS58142767A/en
Publication of JPS58142767A publication Critical patent/JPS58142767A/en
Publication of JPH0410713B2 publication Critical patent/JPH0410713B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/50Methods or arrangements for servicing or maintenance, e.g. for maintaining operating temperature
    • H01M6/5088Initial activation; predischarge; Stabilisation of initial voltage
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/50Methods or arrangements for servicing or maintenance, e.g. for maintaining operating temperature
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Primary Cells (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はリチウムを負極活物質とし、二酸化マ
ンガンを正極活物質とする有機電解質電池の製造
法の改良に係り、内部抵抗が小さくかつ貯蔵性能
が良好な有機電解質電池を提供することを目的と
する。 負極活物質としてリチウムを用い、電解液とし
て各種の有機溶媒に過塩素酸塩、ホウフツ化塩な
どの溶質を溶解させた有機電解質を用いる有機電
解質電池においては、正極活物質として貯蔵中で
の溶解が少なく、かつ単極電位の高い二酸化マン
ガンが好用されているが、この二酸化マンガンを
正極活物質として用いた有機電解質電池は、貯蔵
中に内部抵抗が増加するという問題がある。 そこで、本発明者らは、その原因を究明すべく
種々検討を重ねたところ、貯蔵中における内部抵
抗の増加は、放電初期に現われる二酸化マンガン
の高電位部分が電解液を酸化することによつて引
きおこされることが判明した。 そのため、本発明者らはそのような二酸化マン
ガンの高電位部分を消去すべく鋭意研究を重ね、
電池組立後に10〜25mA/cm2の定電流で予備放電
するときには、二酸化マンガンの高電位部分が消
去されて貯蔵中の内部抵抗の増加が抑制されると
ともに、リチウム表面の酸化皮膜も除去されて、
内部抵抗が小さくかつ貯蔵性能が良好な有機電解
質電池が得られることを見出し、それについて既
に特許出願(特願昭56−167759号)をしたが、さ
らに研究を重ねた結果、直流定電流に交流電流を
重畳して予備放電するときは、直流電流のみで予
備放電する場合に比べて小さい電流でかつ少ない
予備放電電気量で内部抵抗が小さくかつ貯蔵性能
が良好な有機電解質電池が得られることを見出
し、本発明を完成するにいたつた。 すなわち、本発明はリチウムを負極活物質と
し、二酸化マンガンを正極活物質とする有機電解
質電池を製造するにあたり、電池組立後、5〜25
mA/cm2の直流定電流に交流電流を合成電流の極
性が反転しない範囲で重畳して予備放電すること
を特徴とする有機電解質電池の製造法に関する。 直流定電流に交流電流を重畳することにより、
直流定電流のみで予備放電する場合に比べて小さ
い電流でかつ少ない放電電気量で内部抵抗が小さ
く貯蔵性能が良好な有機電解質電池が得られる理
由は、現在のところ必ずしも明確ではないが、交
流電流の重畳により電流が周期的に強弱するの
で、リチウム表面の酸化皮膜の除去が容易にな
り、かつ二酸化マンガンの還流が粉体深部にまで
行われることによるものと考えられる。 重畳する交流電流の周波数は電池の大きさ、形
状、正極の組成、電解液の種類などによつても異
なるが0.5〜100Hzの範囲が好ましい。また重畳す
る交流電流の電流値は、直流定電流が5〜25m
A/cm2の範囲から選ばれるので、それに応じて合
成電流の極性を反転しない範囲内で選択すればよ
い。 本発明において直流定電流の範囲を5〜25m
A/cm2としたのは、直流電流が上記範囲より大き
くなると電池反応以外に電解液の酸化などの副反
応が生じるからであり、また上記範囲より小さく
なるとリチウム表面の酸化皮膜の除去がリチウム
表面の全面から行われずに部分的に行われ、開路
電圧は低下するが、残存した酸化皮膜により内部
抵抗が充分に小さくならないからである。なお、
本発明において、この5〜25mA/cm2という定電
流値は負極リチウムの正極側に対向する面積を基
にしたものである。 本発明において、予備放電電気量は正極容量の
1.5〜5%とするのが好ましい。これはこの程度
予備放電すると二酸化マンガンの高電位部分の消
去が充分にでき、電解液の酸化が充分に防止でき
ることと、この程度の予備放電では実用的に許容
できる放電容量を電池が保持しうるからである。
すなわち、本発明者らの研究によれば、二酸化マ
ンガンが電解液を酸化する電位の下限は3.08V付
近にあり、予備放電電気量が前記範囲より少ない
場合は電圧が3.08V付近まで低下せず、そのため
電解液が酸化されるおそれがあり、また予備放電
電気量が前記範囲より多くなると放電容量の損失
が大きくなるからである。 そして、本発明において電解液としては、たと
えば炭酸プロピレン、γ−ブチロラクトン、テト
ラヒドロフラン、1,2−ジメトキシエタン、ジ
オキソランなどの単独または2種以上の混合溶媒
に過塩素酸リチウム、ホウフツ化リチウムなどの
電解質を溶解させたものが使用される。 つぎに実施例をあげて本発明を説明する。 400℃で4時間熱処理した二酸化マンガン100部
(重量部、以下同様)、りん状黒鉛10部およびポリ
テトラフルエオルチレン2部からなる混合物290
mgを金型に充填し、1t/cm2で予備成形したのち、
該予備成形体上にステンレス鋼製網を配置し、
7t/cm2で直径16mm、厚さ0.5mmに加圧成形し、こ
れを正極とする。 上記正極と、直径14mm、厚さ0.2mmのリチウム
板よりなる負極と、炭酸プロピレンと1,2−ジ
メトキシエタンとの容量比が1:1の混合溶媒に
過塩素酸リチウムを0.5モル/溶解させた電解
液とを用い、第1図に示すような構成で直径20
mm、厚さ1.6mmの扁平形の有機電解質電池を常法
により組み立てた。なお、第1図において、1は
前記の正極、2はステンレス鋼製網であり、3は
ステンレス鋼製の正極缶である。4はポリプロピ
レン不織布からなるセパレータで、5はステンレ
ス鋼製の負極缶である。6は負極缶5の内面にス
ポツト溶接したステンレス鋼製網で、7は前記の
負極であり、上記網6に圧着されている。8はポ
リプロピレン製の環状ガスケツトである。 前記のように組み立てた電池をガルバノスタツ
トとフアンクシヨンゼネレータとにより第1表に
示す直流定電流に周波数5Hzで振幅50%の交流電
流を重畳して正極容量の3.5%予備放電し、予備
放電後の電池の初度および60℃で所定期間貯蔵後
の内部抵抗(20℃における内部抵抗、以下同様)
を測定した。その結果を第1表に示す。 比較のため、先願法すなわち直流定電流のみで
予備放電した場合の結果を第1表に併せて記載す
る。
The present invention relates to an improvement in the manufacturing method of an organic electrolyte battery using lithium as a negative electrode active material and manganese dioxide as a positive electrode active material, and aims to provide an organic electrolyte battery with low internal resistance and good storage performance. . In organic electrolyte batteries that use lithium as the negative electrode active material and an organic electrolyte in which solutes such as perchlorate and borofluoride salts are dissolved in various organic solvents as the electrolyte, dissolution during storage as the positive electrode active material Manganese dioxide, which has a small amount of carbon dioxide and a high monopolar potential, is preferably used, but organic electrolyte batteries using this manganese dioxide as a positive electrode active material have a problem in that internal resistance increases during storage. Therefore, the inventors of the present invention conducted various studies to investigate the cause, and found that the increase in internal resistance during storage is due to the high potential part of manganese dioxide that appears at the beginning of discharge oxidizing the electrolyte. It turned out to be triggered. Therefore, the present inventors have conducted extensive research to eliminate such high potential parts of manganese dioxide, and
When predischarging at a constant current of 10 to 25 mA/cm 2 after battery assembly, the high potential part of the manganese dioxide is erased, suppressing the increase in internal resistance during storage, and the oxide film on the lithium surface is also removed. ,
He discovered that it was possible to obtain an organic electrolyte battery with low internal resistance and good storage performance, and had already applied for a patent (Japanese Patent Application No. 167759, 1983) for this, but as a result of further research, he discovered that it was possible to obtain an organic electrolyte battery with low internal resistance and good storage performance. When pre-discharging with superimposed currents, an organic electrolyte battery with low internal resistance and good storage performance can be obtained with a smaller current and smaller amount of pre-discharge electricity than when pre-discharging with only DC current. This led to the completion of the present invention. That is, in manufacturing an organic electrolyte battery in which lithium is used as a negative electrode active material and manganese dioxide is used as a positive electrode active material, the present invention provides a method for manufacturing an organic electrolyte battery using lithium as a negative electrode active material and manganese dioxide as a positive electrode active material.
The present invention relates to a method for producing an organic electrolyte battery, characterized in that preliminary discharge is carried out by superimposing an alternating current on a constant direct current of mA/cm 2 within a range in which the polarity of the combined current is not reversed. By superimposing alternating current on constant direct current,
It is currently not clear why an organic electrolyte battery with low internal resistance and good storage performance can be obtained with a smaller current and a smaller amount of discharged electricity than when pre-discharging with only a constant DC current, but This is thought to be due to the fact that the electric current periodically changes in strength due to the superposition of the ions, which makes it easier to remove the oxide film on the lithium surface, and refluxes the manganese dioxide deep into the powder. The frequency of the superimposed alternating current varies depending on the size and shape of the battery, the composition of the positive electrode, the type of electrolyte, etc., but is preferably in the range of 0.5 to 100 Hz. Also, the current value of the superimposed alternating current is 5 to 25 m when the direct current is constant.
Since it is selected from the range of A/cm 2 , it may be selected within a range that does not reverse the polarity of the composite current. In the present invention, the range of DC constant current is 5 to 25 m.
The reason for setting A/ cm2 is that if the DC current exceeds the above range, side reactions such as oxidation of the electrolyte will occur in addition to the battery reaction, and if the DC current falls below the above range, the removal of the oxide film on the lithium surface will be difficult. This is because, although the open-circuit voltage is lowered because it is applied to a portion of the surface rather than the entire surface, the internal resistance is not sufficiently reduced due to the remaining oxide film. In addition,
In the present invention, this constant current value of 5 to 25 mA/cm 2 is based on the area of the negative electrode lithium facing the positive electrode side. In the present invention, the pre-discharge electricity amount is equal to the positive electrode capacity.
It is preferably 1.5 to 5%. This is because pre-discharging to this extent can sufficiently erase the high potential portion of manganese dioxide and sufficiently prevent oxidation of the electrolyte, and this pre-discharging can also allow the battery to maintain a practically acceptable discharge capacity. It is from.
That is, according to the research of the present inventors, the lower limit of the potential at which manganese dioxide oxidizes the electrolyte is around 3.08V, and if the amount of pre-discharge electricity is less than the above range, the voltage will not drop to around 3.08V. Therefore, there is a risk that the electrolytic solution will be oxidized, and if the amount of electricity for preliminary discharge exceeds the above range, the loss of discharge capacity will increase. In the present invention, the electrolytic solution includes, for example, a solvent such as propylene carbonate, γ-butyrolactone, tetrahydrofuran, 1,2-dimethoxyethane, dioxolane, etc. alone or a mixture of two or more thereof, and an electrolyte such as lithium perchlorate or lithium borofluoride. A dissolved solution is used. Next, the present invention will be explained with reference to Examples. Mixture 290 consisting of 100 parts of manganese dioxide (parts by weight, the same applies hereinafter), 10 parts of phosphorous graphite, and 2 parts of polytetrafluoroethylene, heat treated at 400°C for 4 hours.
After filling mg into a mold and preforming at 1t/ cm2 ,
placing a stainless steel mesh on the preform;
Pressure molded at 7t/cm 2 to a diameter of 16mm and thickness of 0.5mm, and use this as the positive electrode. The above positive electrode, a negative electrode made of a lithium plate with a diameter of 14 mm and a thickness of 0.2 mm, and 0.5 mole of lithium perchlorate were dissolved in a mixed solvent of propylene carbonate and 1,2-dimethoxyethane in a volume ratio of 1:1. using an electrolyte with a diameter of 20 mm using the configuration shown in Figure 1.
A flat organic electrolyte battery with a diameter of 1.6 mm and a thickness of 1.6 mm was assembled using a conventional method. In addition, in FIG. 1, 1 is the above-mentioned positive electrode, 2 is a stainless steel mesh, and 3 is a stainless steel positive electrode can. 4 is a separator made of polypropylene nonwoven fabric, and 5 is a negative electrode can made of stainless steel. 6 is a stainless steel mesh spot welded to the inner surface of the negative electrode can 5; 7 is the negative electrode, which is crimped to the mesh 6; 8 is an annular gasket made of polypropylene. The battery assembled as described above is pre-discharged to 3.5% of the positive electrode capacity by superimposing an alternating current with a frequency of 5 Hz and an amplitude of 50% on the constant DC current shown in Table 1 using a galvanostat and a function generator. Internal resistance of the battery initially after discharge and after storage for a specified period at 60℃ (internal resistance at 20℃, same below)
was measured. The results are shown in Table 1. For comparison, Table 1 also shows the results obtained when preliminary discharge was performed using the method of the prior application, that is, using only a constant DC current.

【表】 第1表に示すように、交流電流を重畳する場合
は直流電流が5〜25mA/cm2の範囲で内部抵抗が
小さく、かつ貯蔵による内部抵抗増加が少ない。
なお直流電流のみで予備放電する先願法も良好な
効果を発揮するが、先願法の場合10〜25mA/cm2
の範囲で内部抵抗が小さく、貯蔵による内部抵抗
増加が少なくなつており、良好な効果を発揮する
電流値の下限が本発明の方法に比べて若干高いと
ころにある。 つぎに、前記と同様に組み立てた有機電解質電
池を17mA/cm2の直流定電流に周波数5Hzで振幅
50%の交流電流を重畳して第2表に示す電気量予
備放電した。 予備放電後の電池の初度および60℃で所定期間
貯蔵後の内部抵抗を測定した結果を第2表に示
す。 なお第2表中の予備放電電気量は該放電電気量
が正極容量の何パーセントに相当するかで示され
ている。 比較のため、先願法より17mA/cm2の直流定電
流のみで予備放電した場合の結果を第2表に併せ
て記載する。
[Table] As shown in Table 1, when alternating current is superimposed, the internal resistance is small when the direct current is in the range of 5 to 25 mA/cm 2 , and the increase in internal resistance due to storage is small.
Note that the first application method, which pre-discharges only with direct current, also exhibits good effects, but in the first application method, 10 to 25 mA/cm 2
The internal resistance is small in the range of , the increase in internal resistance due to storage is small, and the lower limit of the current value that exhibits good effects is slightly higher than that of the method of the present invention. Next, the organic electrolyte battery assembled in the same manner as above was subjected to a constant DC current of 17 mA/cm 2 with an amplitude of 5 Hz.
A 50% alternating current was superimposed to pre-discharge the amount of electricity shown in Table 2. Table 2 shows the results of measuring the internal resistance of the battery initially after preliminary discharge and after storage at 60° C. for a predetermined period. Note that the pre-discharged electricity amount in Table 2 is indicated by the percentage of the positive electrode capacity that the discharged electricity amount corresponds to. For comparison, Table 2 also shows the results obtained when preliminary discharge was performed using only a constant DC current of 17 mA/cm 2 according to the method of the prior application.

【表】 第2表に示すように、交流電流を重畳する場合
は正極容量の1.5%以上予備放電すれば、内部抵
抗が小さく、かつ貯蔵による内部抵抗増加が充分
に小さくなる。なお先願法でも良好な効果を発揮
するが、先願法の場合予備放電電気量が2%以上
で内部抵抗増加が特に少なくなつており、良好な
効果を発揮する予備放電電気量の下限が本発明の
方法に比べて若干高いところにある。
[Table] As shown in Table 2, when alternating current is superimposed, if the positive electrode capacity is pre-discharged by 1.5% or more, the internal resistance will be small and the increase in internal resistance due to storage will be sufficiently small. Note that the first application method also exhibits a good effect, but in the case of the first application method, the increase in internal resistance is particularly small when the amount of pre-discharge electricity is 2% or more, and the lower limit of the amount of pre-discharge electricity that exhibits a good effect is This is slightly higher than the method of the present invention.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の有機電解質電池の実施例を示
す断面図である。 1……正極、7……負極。
FIG. 1 is a sectional view showing an embodiment of the organic electrolyte battery of the present invention. 1...Positive electrode, 7...Negative electrode.

Claims (1)

【特許請求の範囲】 1 リチウムを負極活物質、二酸化マンガンを正
極活物質とし、電池組立後、5〜25mA/cm2の直
流定電流に交流電流を合成電流の極性が反転しな
い範囲で重畳して予備放電することを特徴とする
有機電解質電池の製造法。 2 予備放電電気量が正極容量の1.5〜5%であ
る特許請求の範囲第1項記載の有機電解質電池の
製造法。
[Scope of Claims] 1. Lithium is used as a negative electrode active material and manganese dioxide is used as a positive electrode active material, and after battery assembly, an alternating current is superimposed on a constant direct current of 5 to 25 mA/cm 2 to the extent that the polarity of the combined current is not reversed. A method for producing an organic electrolyte battery characterized by pre-discharging. 2. The method for manufacturing an organic electrolyte battery according to claim 1, wherein the pre-discharge amount of electricity is 1.5 to 5% of the positive electrode capacity.
JP57026354A 1982-02-20 1982-02-20 Manufacture of organic electrolyte battery Granted JPS58142767A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57026354A JPS58142767A (en) 1982-02-20 1982-02-20 Manufacture of organic electrolyte battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57026354A JPS58142767A (en) 1982-02-20 1982-02-20 Manufacture of organic electrolyte battery

Publications (2)

Publication Number Publication Date
JPS58142767A JPS58142767A (en) 1983-08-24
JPH0410713B2 true JPH0410713B2 (en) 1992-02-26

Family

ID=12191131

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57026354A Granted JPS58142767A (en) 1982-02-20 1982-02-20 Manufacture of organic electrolyte battery

Country Status (1)

Country Link
JP (1) JPS58142767A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6200656B2 (en) * 2013-02-22 2017-09-20 Fdk株式会社 Lithium battery manufacturing method

Also Published As

Publication number Publication date
JPS58142767A (en) 1983-08-24

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