JPH0415585B2 - - Google Patents
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- Publication number
- JPH0415585B2 JPH0415585B2 JP57026355A JP2635582A JPH0415585B2 JP H0415585 B2 JPH0415585 B2 JP H0415585B2 JP 57026355 A JP57026355 A JP 57026355A JP 2635582 A JP2635582 A JP 2635582A JP H0415585 B2 JPH0415585 B2 JP H0415585B2
- Authority
- JP
- Japan
- Prior art keywords
- current
- positive electrode
- discharge
- internal resistance
- organic electrolyte
- 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 - Lifetime
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Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/50—Methods or arrangements for servicing or maintenance, e.g. for maintaining operating temperature
- H01M6/5088—Initial activation; predischarge; Stabilisation of initial voltage
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/50—Methods or arrangements for servicing or maintenance, e.g. for maintaining operating temperature
-
- 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
- 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
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こと
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
らに研究に重ねた結果、直流定電流に該定電流値
よりも大きな振幅をもつた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
気量で前記の効果が達成される上に、重負荷放電
性能も改良されることを見出し、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〜
25mA/cm2の直流定電流に該定電流値よりも大き
な振幅をもつた交流電流を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。
直流定電流に該定電流値よりも大きな振幅をも
つた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
マンガンの還元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。そして重負荷放電性能が
向上するのは、電流の反転部すなわち電流が負に
なる部分でリチウムの電析が行われ、表面がデン
ドライト状になつて反応面積が大きくなることに
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
する交流電流の振幅は大きすぎると電析リチウム
の脱落により、かえつて反応面積が減少して閉路
電圧が低下するので、直流定電流値よりは大きく
てかつ直流定電流値の2.5倍以下が好ましい。
本発明において直流定電流の範囲を5〜
25mA/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
テトラフルオルエチレン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1.5倍の交流
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, lithium is used as the positive electrode active material during storage. Manganese dioxide, which has low dissolution and 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 also removing the oxide film on the lithium surface. Been,
It was discovered that an organic electrolyte battery with low internal resistance and good storage performance could be obtained, and a patent application (Japanese Patent Application No. 167759, 1983) was filed for this, but as a result of further research, it was found that an organic electrolyte battery with low internal resistance and good storage performance could be obtained. When pre-discharging is performed by superimposing an alternating current with a larger amplitude than the constant current value, the above effect is achieved with a smaller current and with a smaller amount of pre-discharge electricity than when pre-discharging with only direct current. In addition, the inventors have discovered that heavy load discharge performance is also improved, leading 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 5 to 5 steps after battery assembly.
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 having an amplitude larger than the constant current value on a direct current constant current of 25 mA/cm 2 . By superimposing an alternating current with a larger amplitude than the constant current value on a constant DC current, the internal resistance is small and the storage performance is reduced with a smaller current and a smaller amount of discharged electricity than when pre-discharging with only a constant DC current. The reason why an organic electrolyte battery with good performance can be obtained is not entirely clear at present, but since the current is periodically strengthened and weakened by superimposing alternating current, the oxide film on the lithium surface can be easily removed, and the manganese dioxide This is thought to be due to the reduction occurring deep within the powder. It is thought that the reason why the heavy load discharge performance is improved is that lithium is deposited at the current reversal part, that is, the part where the current becomes negative, and the surface becomes dendrite-like and the reaction area increases. 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. Furthermore, if the amplitude of the superimposed alternating current is too large, the electrodeposited lithium will fall off, which will reduce the reaction area and lower the closed circuit voltage, so it must be larger than the constant DC current value and less than 2.5 times the constant DC current value. is preferred. In the present invention, the range of DC constant current is 5 to 5.
The reason why the DC current is set at 25 mA/cm 2 is because if the DC current is larger than the above range, side reactions such as oxidation of the electrolyte will occur in addition to the battery reaction, and if it is smaller than the above range, it will be difficult to remove the oxide film on the lithium surface. It is not done from all over the surface, but only partially,
This is because although the open circuit voltage decreases, the internal resistance does not become sufficiently small due to the remaining oxide film. In the present invention, the 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 of 1.5 times the amplitude at a frequency of 5 Hz on the constant DC current shown in Table 1 using a galvanostat and a function generator. The internal resistance (internal resistance at 20°C, hereinafter the same) of the battery initially after discharge and after storage at 60°C for a predetermined period 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
1.5倍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、先願法により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 earlier application method, which pre-discharges only with direct current, also exhibits good effects, but in the earlier application method, the internal resistance is small in the range of 10 to 25 mA/cm 2 , and the increase in internal resistance due to storage is small, so it is good. The lower limit of the current value that exhibits this effect 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 1.5 times as much 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。
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で第3
表に示す振幅の交流電流を重畳して正極容量の
3.5%予備放電した。
予備放電後の電池の80%放電時の−10℃、負荷
300Ωで5秒放電後の閉路電圧を測定した。その
結果を第3表に示す。
比較のため、先願法により17mA/cm2の直流定
電流のみで予備放電した場合の結果を第3表に併
せて記載する。[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 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 at a frequency of 5 Hz.
The positive electrode capacity is calculated by superimposing alternating current with the amplitude shown in the table.
3.5% pre-discharge. -10℃, load at 80% discharge of battery after pre-discharge
The closed circuit voltage was measured after discharging at 300Ω for 5 seconds. The results are shown in Table 3. For comparison, Table 3 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】【table】
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)
極活物質とし、電池組立後、5〜25mA/cm2の直
流定電流に該定電流値よりも大きな振幅をもつた
交流電流を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 with an amplitude larger than the constant current value is applied to a constant current of 5 to 25 mA/cm 2 . A method for manufacturing an organic electrolyte battery characterized by superimposed preliminary discharge. 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57026355A JPS58142768A (en) | 1982-02-20 | 1982-02-20 | Manufacture of organic electrolyte battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57026355A JPS58142768A (en) | 1982-02-20 | 1982-02-20 | Manufacture of organic electrolyte battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58142768A JPS58142768A (en) | 1983-08-24 |
| JPH0415585B2 true JPH0415585B2 (en) | 1992-03-18 |
Family
ID=12191162
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57026355A Granted JPS58142768A (en) | 1982-02-20 | 1982-02-20 | Manufacture of organic electrolyte battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58142768A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52155327A (en) * | 1976-06-21 | 1977-12-23 | Yuasa Battery Co Ltd | Miniature silver peroxide battery |
-
1982
- 1982-02-20 JP JP57026355A patent/JPS58142768A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58142768A (en) | 1983-08-24 |
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