JPS605528B2 - Method for producing silver peroxide - Google Patents
Method for producing silver peroxideInfo
- Publication number
- JPS605528B2 JPS605528B2 JP55182846A JP18284680A JPS605528B2 JP S605528 B2 JPS605528 B2 JP S605528B2 JP 55182846 A JP55182846 A JP 55182846A JP 18284680 A JP18284680 A JP 18284680A JP S605528 B2 JPS605528 B2 JP S605528B2
- Authority
- JP
- Japan
- Prior art keywords
- cadmium
- tellurium
- silver peroxide
- silver
- peroxide
- 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
Links
Classifications
-
- 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
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】
この発明は自己放電性が特に少なく電池用としてすぐれ
た過酸化銀の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing silver peroxide which has particularly low self-discharge properties and is excellent for use in batteries.
電池用過酸化銀はたとえば、時計などに使用する電池に
適するように長い寿命を有することが必要で、このため
には安定性、すなわち自己放電性が少ないことが要求さ
れる。Silver peroxide for batteries needs to have a long life so as to be suitable for batteries used in watches and the like, and for this purpose, it is required to have stability, that is, low self-discharge properties.
電池の保存中に電解液であるアルカリ液中で過酸化銀は
徐々に分解して酸素を放出するが、このとき過酸化銀の
安定性が悪いと保存中に分解が進行し、使用可能電力が
減少し、また分解により生成する酸素の圧力によって気
密にしてあるセルの変形、破損の原因となる。過酸化銀
の製造方法として、硝酸銀溶液と酸化剤とを水酸化アル
カリ液中に加えて過酸化銀を沈殿させる方法が一般に行
われている。During battery storage, silver peroxide gradually decomposes in the alkaline electrolyte and releases oxygen; however, if the stability of silver peroxide is poor, decomposition progresses during storage, reducing the usable power. In addition, the pressure of oxygen produced by decomposition causes deformation and damage to the airtight cell. A commonly used method for producing silver peroxide is to add a silver nitrate solution and an oxidizing agent to an alkaline hydroxide solution to precipitate silver peroxide.
電池用過酸化銀の安定性を表わす尺度として、ガス発生
率または酸素発生率と呼ばれる特性値がある。As a measure of the stability of silver peroxide for batteries, there is a characteristic value called gas generation rate or oxygen generation rate.
これはたとえば、通常の使用状態よりも苛酷な条件を用
い、4ぴ○で40%水酸化ナトリウムまたは水酸化カリ
ウム溶液中に存在する過酸化銀1夕から一定時間に発生
する酸素量で表わされる。過酸化銀電池は電解液として
一般には水酸化ナトリウムが使用されているが、一時に
大電流を必要とする用途のためには水酸化カリウムを電
解液として用いることが必要である。通常得られろ過酸
化銀は水酸化カリウム電解液中では水酸化ナトリウム電
解液中におけるよりも安定性がかなり悪い。過酸化銀を
不安定とする原因は過酸化銀の活性が大きく、これと接
するアルカリ性電解液と反応することによるものと考え
られ、この欠点を除くために過酸化銀粒子の表面を鉛酸
銀で被覆することが米国特許第3017448号明細書
に記載されている。This is expressed, for example, as the amount of oxygen generated in a given time from silver peroxide present in a 40% sodium hydroxide or potassium hydroxide solution at 4 pi . Silver peroxide batteries generally use sodium hydroxide as the electrolyte, but for applications that require a large current at one time, it is necessary to use potassium hydroxide as the electrolyte. The commonly obtained filtered silver oxide is much less stable in potassium hydroxide electrolytes than in sodium hydroxide electrolytes. The reason why silver peroxide becomes unstable is thought to be due to the high activity of silver peroxide, which reacts with the alkaline electrolyte that comes into contact with it. coating is described in US Pat. No. 3,017,448.
この方法は過酸化銀に対し0.1〜5重量%の鉛、酸化
鉛、水酸化鉛または亜ナマリ酸ナトリウムの微粉末を混
合し、アルカリ電解液中で反応させて、過酸化銀の粒子
表面に鉛酸銀を生成させる方法である。この池簿開昭5
4一132732号公報ないし椿関昭54−13273
4号公報には過酸化銀の安定性の改善のためにそれぞれ
Zn、Cd、AIの添加を行うという記載があり、さら
にV、Cr等の添加によってもある程度の効果を示すこ
とが知られている。しかしながらこれらの添加物の効果
は添加剤がないときに比して、酸素発生量が1/2〜1
/3に減少する程度で、40qo、40%水酸化カリウ
ム液中ではいずれも3執そ/夕・4朝時間以上であった
。出願人は先に、同じ目的のために特順昭54一103
1ぞ号および特願昭54−84427号においてそれぞ
れ鉛およびテルル、鉛およびアルミニウムの添加の効果
を開示し、特に後者の場合には不安定度が水酸化ナトリ
ウムよりも大きい水酸化カリウム液中においてさえ従来
のものに例を見ないすぐれた安定性のある過酸化銀が得
られることを報告した。発明者等は酸素発生量をさらに
飛躍的に低減させる方法について研究し、一旦生成した
過酸化銀に金属としてカドミウム成分を0.0丸重量%
以上およびテルル成分を0.01重量%以上で、かつC
dノTeの含有比が0・5以上となるように添加する方
法を特磯昭55一83974号として出願した。発明者
等はさらにカドミウム成分およびテルル成分の添加方法
について鋭意研究の結果、一旦生成した過酸化銀にカド
ミウム成分〜テルル成分を加える代りに過酸化銀の反応
原料または反応工程中に加えてもほぼ同様に過酸化銀の
安定性が向上することを見出して本発明に到達した。す
なわちこの発明は電池用過酸化銀の製造方法としてたと
えば一般に用いられる水酸化アルカリと硝酸銀と酸化剤
で反応させる製造方法において、その反応原料である硝
酸銀水溶液、苛性アルカリ水溶液、酸化剤の少なくとも
1つに予めカドミウム成分とテルル成分とを添加してお
いて反応させて、カドミウムおよびテルルを含有した過
酸化銀とするか、或いは過酸化銀の反応工程中、すなわ
ち中和工程、酸化工程、アルカリ洗篠工程などのいずれ
かにカドミウム成分およびテルル成分を添加することに
よってカドミウムおよびテルルを含有した過酸化銀とす
るもので、過酸化銀中に金属としてカドミウム成分を0
.03重量%以上、およびテルル成分を0.01重量%
でかつCd/Teの含有比が0・5以上となる量で含有
させるように構成したものである。In this method, 0.1 to 5% by weight of lead, lead oxide, lead hydroxide, or sodium malite fine powder is mixed with silver peroxide, and the mixture is reacted in an alkaline electrolyte to form silver peroxide particles. This method generates lead acid silver on the surface. This Ikebo Kaisho 5
Publication No. 4-132732 or Tsubaki Sekisho 54-13273
Publication No. 4 describes the addition of Zn, Cd, and AI to improve the stability of silver peroxide, and it is also known that the addition of V, Cr, etc. has some effect. There is. However, the effect of these additives is that the amount of oxygen generated is 1/2 to 1/2 compared to when no additives are used.
In the 40 qo, 40% potassium hydroxide solution, it was more than 3 times per evening and 4 times in the morning. The applicant had previously applied for the same purpose under the Special Order No. 54-103.
No. 1 and Japanese Patent Application No. 1984-84427 disclose the effects of adding lead and tellurium, and lead and aluminum, respectively, and especially in the latter case, the instability in potassium hydroxide solution is greater than that of sodium hydroxide. It was reported that silver peroxide with excellent stability unparalleled in the past could be obtained. The inventors researched a method to further dramatically reduce the amount of oxygen generated, and added 0.0% by weight of cadmium as a metal to silver peroxide once generated.
and the tellurium component is 0.01% by weight or more, and C
A method of adding d-Te so that the content ratio becomes 0.5 or more was filed as Tokuiso Sho 55-83974. Furthermore, as a result of intensive research into the method of adding cadmium and tellurium components, the inventors found that instead of adding cadmium to tellurium components to silver peroxide once produced, they could be added to the reaction raw materials for silver peroxide or during the reaction process. The present invention was achieved by discovering that the stability of silver peroxide was similarly improved. That is, this invention relates to a manufacturing method for producing silver peroxide for batteries, for example, in which alkali hydroxide, silver nitrate, and an oxidizing agent are reacted, which is generally used. A cadmium component and a tellurium component are added in advance and reacted to produce silver peroxide containing cadmium and tellurium, or during the reaction process of silver peroxide, that is, a neutralization process, an oxidation process, and an alkali washing process. Silver peroxide containing cadmium and tellurium is produced by adding cadmium and tellurium components to either the Shino process or the like, and the cadmium component is removed as a metal in silver peroxide.
.. 03% by weight or more, and tellurium component by 0.01% by weight
and the content ratio of Cd/Te is 0.5 or more.
さらにはカドミウム成分あるいはテルル成分の一方を反
応原料に、他方を反応工程中に添加しても、また反応原
料と反応工程中の両方に添加してもよい。Further, one of the cadmium component and the tellurium component may be added to the reaction raw material and the other during the reaction process, or may be added to both the reaction raw material and the reaction process.
この発明は従来公知の他の製造方法、例えばハロゲン化
銀酸化法、オゾン酸化法等に適用してもその効果に若干
のバラッキはあるが、いずれもその安定性を改善し、ガ
ス発生率を減少できる。Even when this invention is applied to other conventionally known manufacturing methods, such as silver halide oxidation method and ozone oxidation method, the effectiveness varies slightly, but all of them improve the stability and reduce the gas generation rate. Can be reduced.
過酸化銀に含有させるカドミウム成分およびテルル成分
は金属としてカドミウムは0.0箱重量%以上、テルル
は0.01重量%以上で、かつCd/Teの比が0.5
以上が必要である。両成分の下限添加量であるカドミウ
ム0.03重量%と、テルル0.01重量%の組合せ使
用の場合でもカドミウムを単独で使用する従来技術に較
べて過酸化銀の安定効果を著しく改善する。同等の効果
を求めるためにはカドミウムを0.立重量%以上使用す
る必要があることから明らかに両成分使用による相乗効
果を示すものと考えられる。カドミウムおよびテルルを
併用する場合の酸素発生量の減少効果は勿論無添加試料
に較べて充分有効であるが、それぞれの含有量が上記下
限添加量以下であるとその効果の顕著性は不充分となる
。さらに、含有させるCd/Teの比を0.5以上に保
つことが必要で、前記比が0.5以下、すなわちテルル
量がカドミウム量の2倍以上となるとかえってその効果
を減ずることになるので好ましくない。The cadmium component and tellurium component contained in silver peroxide are metals such that cadmium is 0.0% by weight or more, tellurium is 0.01% by weight or more, and the Cd/Te ratio is 0.5.
The above is necessary. Even when using a combination of 0.03% by weight of cadmium and 0.01% by weight of tellurium, which is the lower limit addition amount of both components, the stabilizing effect of silver peroxide is significantly improved compared to the conventional technique in which cadmium is used alone. To obtain the same effect, cadmium should be added to 0. Since it is necessary to use more than % by weight, it is considered that the use of both components clearly shows a synergistic effect. Of course, the effect of reducing the amount of oxygen generated when using cadmium and tellurium in combination is sufficiently effective compared to samples without additives, but if the content of each is below the above lower limit addition amount, the effect may not be sufficiently noticeable. Become. Furthermore, it is necessary to maintain the Cd/Te ratio to be contained at 0.5 or more; if the ratio is 0.5 or less, that is, the amount of tellurium is more than twice the amount of cadmium, the effect will be reduced. Undesirable.
両成分の使用量の上限はカドミウムおよびテルルの合計
で1の重量%程度とするのが好ましく、過大の使用は過
酸化銀の純度を低下させるために発生電気量の低下を招
くことになる。しかし電池の陽極を形成するための増量
剤として使用するような場合は1.0重量%以上の添加
も可能で、その場合でも過酸化銀の安定性が低下するこ
とはない。添加するカドミウム成分の例としては酸化カ
ドミウム、水酸化カドミウム、金属カドミウム粉、硫化
カドミウム、硫酸カドミウム、硝酸カドミウム、ステア
リン酸カドミウム、蟻酸カドミウムおよびセレン化カド
ミウム等があり、これらは一種または組合せで使用され
る。The upper limit of the amount of both components used is preferably about 1% by weight for the total of cadmium and tellurium; using too much will lower the purity of silver peroxide, leading to a decrease in the amount of electricity generated. However, when used as an extender for forming an anode of a battery, it is possible to add 1.0% by weight or more, and even in this case, the stability of silver peroxide will not decrease. Examples of cadmium components to be added include cadmium oxide, cadmium hydroxide, metal cadmium powder, cadmium sulfide, cadmium sulfate, cadmium nitrate, cadmium stearate, cadmium formate, and cadmium selenide, which may be used alone or in combination. Ru.
また使用するテルル成分の例としては、二酸化テルル、
三酸化テルル、金属テルル粉およびテルル酸、亜テルル
酸またはそれらのアルカリ塩等があり、これらの一種ま
たは組合せで使用できる。またカドミウムとテルルの両
方を含む化合物、合金たとえ‐ばCdTe03、CdT
e04、Cd−Te合金粉末を添加することもできる。Examples of tellurium components used include tellurium dioxide,
There are tellurium trioxide, metal tellurium powder, telluric acid, tellurite acid, or alkali salts thereof, and these can be used alone or in combination. Compounds and alloys containing both cadmium and tellurium, such as CdTe03, CdT
e04, Cd-Te alloy powder can also be added.
テルル成分の場合には苛性アルカリ水溶液に溶解するた
め、添加量全量が過酸化銀中に残留するわけではなく、
添加条件によってはかなり歩蟹りの悪い場合がある。In the case of the tellurium component, it is dissolved in the caustic aqueous solution, so the entire amount added does not remain in the silver peroxide.
Depending on the addition conditions, the performance may be quite poor.
このような場合には予めテルル成分の歩蟹り率を予測し
てその分だけ過剰に加える必要がある。またテルルの歩
蟹りを良くするために反応終了後のアルカリ洗練工程に
加えるのが好ましい。以下この発明を実施例について説
明する。In such a case, it is necessary to predict the yield rate of the tellurium component in advance and add the amount in excess. Further, in order to improve the growth rate of tellurium, it is preferable to add it to the alkali refining step after the reaction is completed. This invention will be described below with reference to embodiments.
実施例 1
A鍋0夕/夕、pH2.0の硝酸銀水溶液1000の‘
にカドミウムおよびテルル成分をCd(OH)2、Te
02の形態にて所定量加え、よく鷹拝して80ooに加
温*し、水酸化ナトリウム400夕/そ水溶液250の
‘を加え、さらに続けて過硫酸カリウム150夕を加え
、そのまま30分間反応させた後、充分額斜、洗糠し、
炉過、乾燥した過酸化銀を試料として水酸化カリウム4
0%水溶液中の40qoでのAgo1夕当りのガス発生
率および製品過酸化銀中のカドミウム、テルルの含有量
を測定した。Example 1 Pot A: 1/2, pH 2.0 silver nitrate aqueous solution 1000'
Add cadmium and tellurium components to Cd(OH)2, Te
Add the specified amount in the form of 02, shake well and heat to 80℃*, add 400mL of sodium hydroxide/250mL of an aqueous solution, then add 150mL of potassium persulfate, and react for 30 minutes. After that, wash the forehead thoroughly and wash the rice bran.
Potassium hydroxide 4 was used as a sample of filtered and dried silver peroxide.
The gas generation rate per night of Ago at 40 qo in a 0% aqueous solution and the contents of cadmium and tellurium in the silver peroxide product were measured.
結果を第1表に示す。第1表
試験No.1〜3は比較例でカドミウムおよびテルルを
全く含有しないか、一方のみ含有するものである。The results are shown in Table 1. Table 1 Test No. Comparative Examples 1 to 3 do not contain cadmium or tellurium at all, or contain only one of them.
試験No.4カドミウムとテルルの両者が添加されては
いるがこの発明の下限以下の添加量のためにガス発生率
の低下が充分でない。試験No.59はこの発明に係る
製品でいずれもガス発生率低下が著しい。試験No.9
は添加量が多い場合であるが、これ以上添加しても効果
は限界であることを示している。試験No.10〜14
はCd/Te比が0.5またはそれ以下の例で、カドミ
ウムの添加量がほぼ等しい試験No.6〜8と比較して
もその効果が顕著でなくなっており、特に試験No.1
4のようにCd、Teの添加量が大きくなるとその煩向
が著しい。実施例 2
100タ′そのNaOH水溶液1000の‘にカドミウ
ム源の所定量を加え、よく燈拝し、これに過硫酸カリウ
ム160夕を加え、75qoに加溢し、A雛00タ′〆
を含有する硝酸銀水溶液165の【を添加して40分間
反応させる。Test No. Although both 4-cadmium and tellurium are added, the amount of addition is below the lower limit of this invention, so the gas generation rate is not sufficiently reduced. Test No. No. 59 is a product according to the present invention, and all of them show a remarkable decrease in gas generation rate. Test No. 9
This is the case when the amount added is large, but it shows that there is a limit to the effect even if added more than this. Test No. 10-14
Test No. 1 is an example in which the Cd/Te ratio is 0.5 or less, and the amount of cadmium added is almost the same. Even when compared with Test Nos. 6 to 8, the effect is no longer noticeable, especially in Test No. 1
As shown in No. 4, when the amounts of Cd and Te added are large, the problem becomes significant. Example 2 A predetermined amount of a cadmium source was added to 100 liters of the NaOH aqueous solution, simmered well, and 160 quarts of potassium persulfate was added to it, and the mixture was made to overflow to 75 quarts, containing 0.00 liters of A-chicken. Add 165% of an aqueous silver nitrate solution and allow to react for 40 minutes.
反応終了後テルル源の所定量を加え、さりこ80ooで
10分間反応させた後、煩斜、洗糠、炉過したものにつ
き水酸化カリウム40%水溶液中の4000でのAgO
1夕当りのガス発生率を測定した。結果を第2表に示す
。第2表
試験No.15〜18に示すように各種のカドミウム源
、テルル源を用いても結果に多少のバラッキはあるが類
似の効果が認められた。After the reaction was completed, a predetermined amount of tellurium source was added, and the reaction was carried out for 10 minutes at 80 oo of saline, followed by washing, washing, and filtering.
The gas generation rate per evening was measured. The results are shown in Table 2. Table 2 Test No. As shown in 15 to 18, similar effects were observed even when various cadmium sources and tellurium sources were used, although there were some variations in the results.
試験No.19 20はガス発生率の試験にNaOHを
用いた成績を示している。Cd/Teの比はいずれも2
.0以上であった。実施例 3
100多′その塩化ナトリウム水溶液500の‘に*C
d○、Te02の所定量を添加、燈拝しながら33夕の
硝酸銀結晶を徐々に加えて塩化銀をつくり、これに50
夕のNaOH結晶を加えて溶解後75qoに調整し、さ
らに過硫酸カリウム粉末30夕を少しづつ加え、3時間
鷹拝しながら反応させる。Test No. 19 and 20 show the results of using NaOH in the gas generation rate test. The Cd/Te ratio is 2 in both cases.
.. It was 0 or more. Example 3 100% of the sodium chloride aqueous solution 500% *C
Add a predetermined amount of d○, Te02, gradually add 33 yen silver nitrate crystals while holding a light to make silver chloride, and add 50 ml of silver chloride to this.
After dissolving the solution, add NaOH crystals to adjust the concentration to 75 quarts, then add 30 quarts of potassium persulfate powder little by little, and let the mixture react for 3 hours while stirring.
生成物を洗練、炉過後660で2幼時間乾燥し実施例2
と同様にガス発生率を測定した。結果を第3表に示す。
第3表上表の結果から塩化銀を経由する過酸化銀の製造
工程に本発明を適用しても大きな効果を示すことが判る
。The product was refined, passed through the oven, and dried for 2 hours at 660°C to produce Example 2.
The gas generation rate was measured in the same manner. The results are shown in Table 3.
From the results shown in Table 3 above, it can be seen that even when the present invention is applied to the production process of silver peroxide via silver chloride, it shows great effects.
Claims (1)
応原料または反応工程中にカドミウム成分およびテルル
成分を添加することから成り、その際、過酸化銀に金属
としてカドミウム成分を0.03重量%以上およびテル
ル成分を0.01重量%以上で、かつCd/Teの含有
比が0.5以上となる量で含有させることを特徴とする
過酸化銀の製造方法。1. A method for producing silver peroxide for batteries, which consists of adding a cadmium component and a tellurium component during the reaction raw material or reaction process of silver peroxide, at which time 0.03 weight of the cadmium component as a metal is added to the silver peroxide. % or more and a tellurium component in an amount of 0.01% by weight or more and a Cd/Te content ratio of 0.5 or more.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55182846A JPS605528B2 (en) | 1980-12-25 | 1980-12-25 | Method for producing silver peroxide |
| US06/271,088 US4338385A (en) | 1980-06-23 | 1981-06-05 | Divalent silver oxide cell containing cadmium and tellurium components |
| GB8118350A GB2079522B (en) | 1980-06-23 | 1981-06-15 | Silver oxide cell |
| CH400781A CH656487A5 (en) | 1980-06-23 | 1981-06-17 | SILVER (II) OXIDE CELL AND METHOD FOR THE PRODUCTION THEREOF. |
| FR8112283A FR2485269A1 (en) | 1980-06-23 | 1981-06-23 | SILVER OXIDE BATTERY DIVALENT, CONTAINING CADMIUM AND TELLURE COMPONENTS |
| DE19813124591 DE3124591C2 (en) | 1980-06-23 | 1981-06-23 | Silver (II) oxide cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55182846A JPS605528B2 (en) | 1980-12-25 | 1980-12-25 | Method for producing silver peroxide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57111241A JPS57111241A (en) | 1982-07-10 |
| JPS605528B2 true JPS605528B2 (en) | 1985-02-12 |
Family
ID=16125475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55182846A Expired JPS605528B2 (en) | 1980-06-23 | 1980-12-25 | Method for producing silver peroxide |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS605528B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6457500A (en) * | 1987-08-28 | 1989-03-03 | Hamamatsu Photonics Kk | Pcd shift register driving device |
| JPH0236409A (en) * | 1988-07-26 | 1990-02-06 | Fanuc Ltd | Power supply system for encoder |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5894761A (en) * | 1981-12-01 | 1983-06-06 | Seiko Instr & Electronics Ltd | Silver peroxide cell |
-
1980
- 1980-12-25 JP JP55182846A patent/JPS605528B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6457500A (en) * | 1987-08-28 | 1989-03-03 | Hamamatsu Photonics Kk | Pcd shift register driving device |
| JPH0236409A (en) * | 1988-07-26 | 1990-02-06 | Fanuc Ltd | Power supply system for encoder |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57111241A (en) | 1982-07-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS605528B2 (en) | Method for producing silver peroxide | |
| JPS5846453B2 (en) | Method for producing silver peroxide | |
| US4338385A (en) | Divalent silver oxide cell containing cadmium and tellurium components | |
| JPS5825083A (en) | Manufacturing method for zinc powder electrodes for primary batteries | |
| US2162385A (en) | Process of manufacturing large surface electrodes | |
| US3615179A (en) | Preparation of magnesium perchlorate | |
| GB2023558A (en) | Process for the Production of Electrochemically Active Lead Dioxide | |
| US3679481A (en) | Process of manufacturing sintered carrier type negative electrodes for alkaline storage cells | |
| CN117228727A (en) | Method for removing calcium and magnesium from manganese sulfate at low cost | |
| JPS6211459B2 (en) | ||
| JPS6031069B2 (en) | silver peroxide battery | |
| JPS61153950A (en) | Zinc alkaline storage battery | |
| JPS58225565A (en) | Alkaline battery | |
| JPS61109256A (en) | Zinc anode of alkaline call | |
| JPH0425670B2 (en) | ||
| JPS62123653A (en) | Zinc-alkaline battery | |
| JPS62123658A (en) | Zinc-alkaline battery | |
| US2191231A (en) | Negative electrode for lead-acid storage batteries and method of producing the same | |
| JPS6141850B2 (en) | ||
| JPS5920602B2 (en) | Production method of silver oxide for batteries | |
| JPS6123707A (en) | Production of zinc alloy powder for negative electrode of alkali battery without addition of mercury | |
| JPH0711955B2 (en) | Non-sintered cadmium cathode for alkaline storage batteries | |
| JPS5832748B2 (en) | Manufacturing method of silver oxide battery | |
| JPS61110963A (en) | Alkaline battery | |
| JPS6027147B2 (en) | Manufacturing method of non-aqueous electrolyte battery |