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JPS5924496B2 - Manufacturing method of positive electrode for silver oxide batteries - Google Patents
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JPS5924496B2 - Manufacturing method of positive electrode for silver oxide batteries - Google Patents

Manufacturing method of positive electrode for silver oxide batteries

Info

Publication number
JPS5924496B2
JPS5924496B2 JP13933576A JP13933576A JPS5924496B2 JP S5924496 B2 JPS5924496 B2 JP S5924496B2 JP 13933576 A JP13933576 A JP 13933576A JP 13933576 A JP13933576 A JP 13933576A JP S5924496 B2 JPS5924496 B2 JP S5924496B2
Authority
JP
Japan
Prior art keywords
ago
silver
positive electrode
battery
silver oxide
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
JP13933576A
Other languages
Japanese (ja)
Other versions
JPS5363537A (en
Inventor
薫 村上
友彦 有田
貢 岡久
泰之 熊野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP13933576A priority Critical patent/JPS5924496B2/en
Publication of JPS5363537A publication Critical patent/JPS5363537A/en
Publication of JPS5924496B2 publication Critical patent/JPS5924496B2/en
Expired legal-status Critical Current

Links

Classifications

    • Y02E60/12

Landscapes

  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 本発明は、二価酸化銀Ag0又はこれと一価酸化銀Ag
20との混合物を正極活物質とし、例えば亜鉛を負極活
物質とする酸化銀電池の正極の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides silver divalent oxide Ag0 or monovalent silver oxide Ag0 and monovalent silver oxide Ag0.
The present invention relates to an improvement in the positive electrode of a silver oxide battery in which a mixture with No. 20 is used as a positive electrode active material and, for example, zinc is used as a negative electrode active material.

従来の小型機器の電力源として、水銀電池あるいは酸化
銀電池がある。
Mercury batteries or silver oxide batteries are conventional power sources for small devices.

そして、最近更に小型化された電子機器の増加に伴い、
電池の大きさが限定され、更に小型で高出力の電池が要
望されてきた。そこで、従来の酸化銀電池の活物質であ
るi]。
And with the recent increase in electronic devices that have become even more compact,
The size of batteries has been limited, and there has been a demand for smaller and higher output batteries. Therefore, the active material of conventional silver oxide batteries is i].

酸化銀Ag2Oに対して、重量当たりの容量にして1.
86倍、容積当たりの容量にして1.93倍の大容量を
取り出せる二価酸化銀(Ag0)が注目されている。し
かし、このAg0は、アルカリ溶液中において不安定で
あり2AgO→Ag3O+1/ 20| のようにAg0よりAg2Oに分解する時の酸素ガス発
生のために、密閉型電池として使用できない問題点があ
つた。
For silver oxide Ag2O, the capacity per weight is 1.
Silver divalent oxide (Ag0) is attracting attention because it can extract 86 times the capacity and 1.93 times the capacity per volume. However, this Ag0 is unstable in an alkaline solution and generates oxygen gas when decomposed from Ag0 to Ag2O as shown in 2AgO→Ag3O+1/20|, so there was a problem that it could not be used as a sealed battery.

そこで、安定したAg0を得るために、アルカリ溶液中
での銀塩の陽極酸化、硝酸銀溶液の電気分解、あるいは
銀塩のオゾン酸化等の製法が提案されているが、密閉型
電池として使用可能な安定したAg0は得られていない
Therefore, in order to obtain stable Ag0, production methods such as anodic oxidation of silver salt in an alkaline solution, electrolysis of silver nitrate solution, or ozone oxidation of silver salt have been proposed, but these methods cannot be used as a sealed battery. Stable Ag0 has not been obtained.

又AgOに酸化鉛PbOの粉末を混入して正極活物質と
する方法、電池構成上のアルカリ電解液に鉛イオンを存
在させその電解液を電池に注液し、AgOの酸素ガス発
生を抑制しようとする試みがなされている。
In addition, there is a method of mixing lead oxide PbO powder into AgO to use as a positive electrode active material, and by making lead ions exist in the alkaline electrolyte in the battery structure and injecting that electrolyte into the battery, it is possible to suppress the generation of oxygen gas from AgO. Attempts are being made to do so.

しかし前者ではその効果が十分認められず、又後者の方
法では電解液中の鋭イオンが負極活物質の亜鉛と反応し
亜鉛極の自己放電を起こすため適切でない。又両者に共
通した問題として、AgO粉末は粉末自身の性質として
非常に成形性が悪く、粉末に何らかの結着剤を混入しな
ければ成形体を作ることが困雌である。通常1〜5重量
%の弗素樹脂を加えているが、この場合でも十分な強度
は得られず、成形体の割れ、端部の欠けを生じている。
本発明は、鉛酸イオンを含んだアルカリ溶液でAg0を
処理することにより、Ag0の分解によるガス発生を効
果的に抑制し、かつ正極の成形性を改良できることを見
出したことに基づくものである。
However, in the former method, the effect is not sufficiently recognized, and in the latter method, sharp ions in the electrolytic solution react with zinc of the negative electrode active material, causing self-discharge of the zinc electrode, so it is not suitable. A common problem with both is that AgO powder itself has very poor moldability, and it is difficult to form a molded body unless some kind of binder is mixed into the powder. Normally, 1 to 5% by weight of fluororesin is added, but even in this case, sufficient strength is not obtained, resulting in cracks in the molded product and chipping at the edges.
The present invention is based on the discovery that by treating Ag0 with an alkaline solution containing lead acid ions, gas generation due to decomposition of Ag0 can be effectively suppressed and the formability of the positive electrode can be improved. .

以下本発明をその実施例により説明する。The present invention will be explained below with reference to Examples.

硝酸銀AgNO35O9を水100TrL1に溶解した
液を調整する。
A solution is prepared by dissolving silver nitrate AgNO35O9 in 100TrL1 of water.

次に水11に709のNaOHを溶解したアルカリ溶液
を温度80′Cに保ち、これに過硫酸カリウムK2S2
O8729を加え終わると同時に、上記AgNO3溶液
を約10分間で滴下する。この時反応容器(フラスコ)
中は攪拌機で一定速度で合成が終わるまで攪拌を続ける
。AgNO3溶液の滴下後約15分間で温度を90゜C
に上げ、同温度に20分間保ちAgNO3のAgO化を
終える。
Next, an alkaline solution containing 709 NaOH dissolved in water 11 was kept at a temperature of 80'C, and potassium persulfate K2S2
At the same time as the addition of O8729 is completed, the above AgNO3 solution is added dropwise for about 10 minutes. At this time, the reaction vessel (flask)
Inside, use a stirrer to continue stirring at a constant speed until the synthesis is complete. After dropping the AgNO3 solution, the temperature was raised to 90°C for about 15 minutes.
and kept at the same temperature for 20 minutes to finish converting AgNO3 into AgO.

次に反応容器中の上澄液を捨て新たに水11を加え5分
間攪拌後、再度その上澄液を捨てる。次に3モル/IO
KOH又はHaOH水溶液11に酸化鉛0.79を溶解
した溶液を上記容器に加え、室温で2時間攪拌後、上澄
液を捨て、次いで水1′を加えて5分間攪拌後上澄液を
捨てる操作を6回繰り返す。
Next, the supernatant liquid in the reaction vessel is discarded, and water 11 is newly added, and after stirring for 5 minutes, the supernatant liquid is discarded again. Then 3 mol/IO
Add a solution of 0.79 lead oxide dissolved in KOH or HaOH aqueous solution 11 to the above container, stir at room temperature for 2 hours, then discard the supernatant, then add water 1' and stir for 5 minutes, then discard the supernatant. Repeat the operation 6 times.

しかる後生成物をろ過し、50゜Cの温度で15時間減
圧乾燥する。こうして表面に銀鉛酸化合物を形成したA
gOを得る。一方電気化学方法によつて.AgOを得る
には、銀ネツトを集電体としその両面に、平均粒度30
ミクロンの銀粉末を2000K9Aゴ程度の田力で加圧
成型して電極を作る。
The product is then filtered and dried under reduced pressure at a temperature of 50° C. for 15 hours. A with a silver lead acid compound formed on the surface in this way
Obtain gO. On the other hand, by electrochemical method. To obtain AgO, a silver net is used as a current collector, and on both sides, an average particle size of 30
Electrodes are made by press-molding micron silver powder using a force of about 2000K9A.

この電極を陽極とし、対極にニツケル又銀板を用いて、
5モル/F.のKOH又はHaOH水溶液中で陽極酸化
する。こうしてAgOにした成型電極を水洗してKOH
又はNaO}{を除いて乾燥した後粉砕し、AgO(7
)粉末を得る。次に前記と同様の方法によりAgO粉末
の表面に銀鉛酸化合物を生成させる。次に上記の化学酸
化法により得たAgO(a)、同じく化学酸化法により
得たAgO粉末に2重量?のPbO粉末を混合したもの
(b)、及び化学酸化法により得たAgO表面に銀鉛酸
化合物2生成させたもの(c)の特性比較結果を説明す
る。
Using this electrode as an anode and a nickel or silver plate as the counter electrode,
5 mol/F. Anodize in KOH or HaOH aqueous solution. The molded electrode made into AgO was washed with water and KOH
Or NaO} {remove and dry, then crush, AgO
) to obtain a powder. Next, a silver lead acid compound is generated on the surface of the AgO powder by the same method as described above. Next, AgO(a) obtained by the above chemical oxidation method, AgO powder also obtained by the chemical oxidation method, and 2 weight? The results of comparing the characteristics of (b) a mixture of PbO powder and (c) a mixture of silver lead acid compound 2 on the surface of AgO obtained by a chemical oxidation method will be explained.

まず各試料19を採取し、内径10.6闘の円筒状成形
型で2000K7の圧力で成形したときの成形厚み及び
成形性は第1表の如くであつた。又各試料に2重量70
の弗素樹脂粉末を結着剤として加え、上記と同様に成形
したペレツトを、温度70′Cの10モル/IKOH水
溶液中に4時間浸漬した場合の平均ガス発生速度は、第
2表の如くであつた。次に前記のペレツトを正極、10
%アマルガム化した粒状亜鉛の成形体を負極として実容
量160mAhのアルカリ電池を構成し、45゜Cの温
度で1力月保存した後、1KΩの抵抗を負荷として放電
したときの電池容量を比較すると第3表のようであつた
First, each sample 19 was taken and molded at a pressure of 2000 K7 using a cylindrical mold with an inner diameter of 10.6 mm.The molding thickness and moldability were as shown in Table 1. Also, 2 weights 70 for each sample.
Table 2 shows the average rate of gas generation when pellets formed in the same manner as above with the addition of fluororesin powder as a binder were immersed in a 10 mol/IKOH aqueous solution at a temperature of 70'C for 4 hours. It was hot. Next, the above pellet was used as a positive electrode,
An alkaline battery with an actual capacity of 160 mAh was constructed using a molded body of amalgamated granular zinc as a negative electrode, and after being stored at a temperature of 45°C for 1 month, the battery capacity was compared when it was discharged with a resistance of 1 KΩ as a load. It looked like Table 3.

以上より明らかなように、化学的に合成したAgOを、
鉛酸イオンを含むアルカリ溶液中で処理することにより
、アルカリ中での分解によるガス発生を少なくすること
ができる。
As is clear from the above, chemically synthesized AgO,
By processing in an alkaline solution containing lead acid ions, gas generation due to decomposition in an alkali can be reduced.

又成形性が改良された結果、電池の組み立てが容易にな
るとともに、電池の体積効率を向上することが可能とな
つた。又第3表のように、化学的に合成したA〆扱びこ
れに銀鉛酸化合物を生成させたものを正極に用いた電池
は、設計どおりの放電容量を示したが、PbO粉末を混
合したAgOを用いた電池及び化学的に合成したAgO
を活物質とし、PbOを溶解した電解液を注液した電池
では放電容量が設計値より少なかつた。
Furthermore, as a result of the improved moldability, it has become possible to assemble the battery easily and improve the volumetric efficiency of the battery. In addition, as shown in Table 3, batteries using chemically synthesized A and a silver lead acid compound as the positive electrode showed discharge capacity as designed, but AgO mixed with PbO powder Batteries using AgO and chemically synthesized AgO
In a battery using PbO as an active material and injecting an electrolyte in which PbO was dissolved, the discharge capacity was lower than the designed value.

これは負極亜鉛の自己放電によるものと考えられる。な
お化学的に合成したAgOの代わりに電気化学的に得た
AgOについても上記と同様である。
This is thought to be due to self-discharge of the negative electrode zinc. Note that the same applies to AgO obtained electrochemically instead of chemically synthesized AgO.

次に、図の曲線1は、化学的に合成したAgOに銀鉛酸
化物を形成するためのアルカリ溶液に溶解したPbOの
濃度と、前記第2表と同様の条件におけるガス発生速度
との関係を示す。同図曲線2はAgO粉末に対するPb
O(7)添加量とガス発生速度との関係を示す。本発明
の方法において、Ag(6)処理するためのアルカリ溶
液に溶解したPbOは、AgO処理によつて殆んどの鉛
分がAgOに添加されるので、アルカリ中のPbO濃度
はAgOに対するPbO添加量として示した。
Next, curve 1 in the figure shows the relationship between the concentration of PbO dissolved in an alkaline solution for forming silver lead oxide on chemically synthesized AgO and the gas generation rate under the same conditions as in Table 2 above. shows. Curve 2 in the same figure is Pb against AgO powder.
The relationship between the amount of O(7) added and the gas generation rate is shown. In the method of the present invention, most of the lead content in the PbO dissolved in the alkaline solution for Ag(6) treatment is added to AgO by the AgO treatment, so the PbO concentration in the alkali is determined by the addition of PbO to AgO. Shown as quantity.

図の曲線1から本発明の方法においてはPbOの量がA
gOlOO9に対して10f!付近で最もガス発生速度
は遅くなるが、銀鉛酸化合物の生成によつて活物質とし
ての利用率が低下するので、0.5〜59Pb0/Ag
OlOO9程度が適当である。
From curve 1 in the figure, in the method of the present invention, the amount of PbO is A
10f for gOlOO9! Although the gas generation rate is slowest in the vicinity, the utilization rate as an active material decreases due to the production of silver lead acid compounds, so 0.5 to 59Pb0/Ag
Approximately OLOO9 is appropriate.

本発明の方法によりAgO表面に生成される銀鉛酸化合
物は、主としてAg5PbO6であつた。上記の実施例
ではAgO単独を正極活物質とする例を示したが、本発
明による処理をしてもガス発生を完全になくするのは困
難である。従つてこれにAg,Oを適当な割合で混合し
て正極活物質とすることは、特に高温で保存した場合の
電池の膨張を少なくする上で有利である。第4表は銀鉛
酸化合物を形成したAgO粉末とAg,O粉末との混合
割合(重量比)を変えた正極を用いた電池を45゜Cで
12時間エージングした後20゜Cで60Ω及び1KΩ
で連続放電したときの放電容量の比較を示す。
The silver lead acid compound produced on the AgO surface by the method of the present invention was mainly Ag5PbO6. In the above embodiment, an example was shown in which AgO alone was used as the positive electrode active material, but even with the treatment according to the present invention, it is difficult to completely eliminate gas generation. Therefore, it is advantageous to mix this with Ag and O in an appropriate ratio to form a positive electrode active material, especially in reducing the expansion of the battery when stored at high temperatures. Table 4 shows that batteries using positive electrodes with different mixing ratios (weight ratios) of AgO powder forming a silver lead acid compound and Ag, O powders were aged at 45°C for 12 hours and then tested at 20°C for 60Ω and 1KΩ
A comparison of the discharge capacity when continuously discharging is shown.

又同表には60゜Cの温度で保存したときの電池の膨張
度合を電池の高さの変化で示した。
The same table also shows the degree of expansion of the battery when stored at a temperature of 60°C as a change in the height of the battery.

なおこの電池は直径11.2mm1高さ4.0關のボタ
ン形電池である。裏 第4表から明らかなように、本発明によるAgOは、適
当な割合でAg2Oと混合して用いることにより、電池
の膨張を少なく、かつAg,O単独を用いるものより電
池容量の大きい実用的な酸化銀電池を得ることができる
Note that this battery is a button type battery with a diameter of 11.2 mm and a height of 4.0 mm. As is clear from Table 4 on the back side, when AgO according to the present invention is mixed with Ag2O in an appropriate proportion, it can be used to reduce battery expansion and provide a practical battery with a larger capacity than a battery using Ag and O alone. A silver oxide battery can be obtained.

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

図面はAgOに対するPbOの添加量とアルカリ溶液中
におけるAgOのガス発生速度との関係を示す。
The drawing shows the relationship between the amount of PbO added to AgO and the gas generation rate of AgO in an alkaline solution.

Claims (1)

【特許請求の範囲】[Claims] 1 二価酸化銀を、鉛酸イオンを含むアルカリ溶液で処
理して、表面に銀鉛酸化合物を形成する工程を有するこ
とを特徴とする酸化銀電池用正極の製造法。
1. A method for producing a positive electrode for a silver oxide battery, comprising the step of treating silver divalent oxide with an alkaline solution containing lead acid ions to form a silver lead acid compound on the surface.
JP13933576A 1976-11-18 1976-11-18 Manufacturing method of positive electrode for silver oxide batteries Expired JPS5924496B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13933576A JPS5924496B2 (en) 1976-11-18 1976-11-18 Manufacturing method of positive electrode for silver oxide batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13933576A JPS5924496B2 (en) 1976-11-18 1976-11-18 Manufacturing method of positive electrode for silver oxide batteries

Publications (2)

Publication Number Publication Date
JPS5363537A JPS5363537A (en) 1978-06-07
JPS5924496B2 true JPS5924496B2 (en) 1984-06-09

Family

ID=15242917

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13933576A Expired JPS5924496B2 (en) 1976-11-18 1976-11-18 Manufacturing method of positive electrode for silver oxide batteries

Country Status (1)

Country Link
JP (1) JPS5924496B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57101350A (en) * 1980-12-16 1982-06-23 Seiko Instr & Electronics Ltd Silver (2) oxide battery
JPS57199177A (en) * 1981-05-31 1982-12-07 Hitachi Maxell Ltd Divalent silver oxide cell

Also Published As

Publication number Publication date
JPS5363537A (en) 1978-06-07

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