JPS6211459B2 - - Google Patents
Info
- Publication number
- JPS6211459B2 JPS6211459B2 JP55140400A JP14040080A JPS6211459B2 JP S6211459 B2 JPS6211459 B2 JP S6211459B2 JP 55140400 A JP55140400 A JP 55140400A JP 14040080 A JP14040080 A JP 14040080A JP S6211459 B2 JPS6211459 B2 JP S6211459B2
- Authority
- JP
- Japan
- Prior art keywords
- silver peroxide
- silver
- cadmium
- added
- component
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/54—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of silver
-
- 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
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Primary Cells (AREA)
Description
この発明は過酸化銀を陽極主剤として用いた過
酸化銀電池の改良に関する。
従来アルカリ電池において陽極に過酸化銀を主
剤とする活物質を用い、陰極に亜鉛等を用いる電
池系は知られているが、過酸化銀は酸化銀などの
他の酸化物と比較して酸素含有量が多いので、こ
れを用いた電池は放電性能が著しく向上する。し
かし過酸化銀は電池内での安定度が小さく、徐々
に酸化銀と酸素な分解するため電池の保存中に発
生した酸素によつて電池の内圧が高くなつて電池
の膨脹または変形が生じ、著しいときには破壊す
る場合もある。このような過酸化銀の分解(自己
放電ともいう)は有効な過酸化銀の量の減少をき
たし、設計通りの電気容量が得られなくなる。と
くに寿命の長い電池ではこの自己放電率の問題は
重要である。
このような過酸化銀電池の欠点を導いている原
因は過酸化銀の活性が大きく、これと接触してい
るアルカリ性電解液との反応によるものと考えら
れる。この欠点を除くため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
細書に記載されており、電池の保存性能は向上し
ている。
発明者等は過酸化銀電池を安定化させることに
つき種々検討の結果、陽極活物質として使用する
過酸化銀を安定化させるために生成した過酸化銀
に種々の添加物を加える試験を行ない、鉛源とア
ルミニウム源を過酸化銀電池の過酸化銀電極また
はアルカリ電解液のいずれかに同時に添加する
と、良好な安定性を示すことを見出して、これを
特願昭54―84427号および特願昭54―84428号とし
て開示した。その後さらにカドミウム成分を過酸
化銀に、テルル成分を過酸化銀または過酸化銀電
池のアルカリ電解液のいずれかに同時に添加する
と飛躍的に安定性がすぐれることを見出して特願
昭55―83974号および特願昭55―99418号の発明に
発展させた。
本発明は上記のカドミウム成分およびテルル成
分を添加した過酸化銀電池に係る発明を更に改良
した発明であつて、カドミウム成分、テルル成分
の添加に加えて、さらに他の特定の元素成分を併
用すると一層すぐれた安定性が得られることを見
出して本発明に到達したのである。
したがつて、この発明の目的は過酸化銀を主剤
として陽極を形成した過酸化銀電池における安定
性が著しく改善された過酸化銀電池を提供するこ
とにある。
この発明によれば、前記過酸化銀電池におい
て、必須成分として過酸化銀にカドミウム成分を
金属として0.03重量%以上、およびテルル成分を
過酸化銀またはアルカリ電解液の少くとも一方に
含有させるほか、さらに選択成分としてタリウ
ム、水銀、鉛、およびゲルマニウムから選ばれる
少くとも1種の成分を含有させてなる過酸化銀電
池が提供される。これらの選択成分のうちタリウ
ム、水銀はアルカリに不溶性であるからその添加
は過酸化銀中に行ない、また鉛、ゲルマニウムは
アルカリに可溶性であるので過酸化銀またはアル
カリ電解液の少くとも一方に含有させればよい。
使用する過酸化銀は硝酸銀水溶液と過硫酸カリ
ウム等の酸化剤とをアルカリ液中で反応させて製
造したものが最も好ましく、他の製造法、たとえ
ば電解酸化法で製造したものでもこの発明を適用
すれば類似の効果を示すが、前者の製造法による
過酸化銀の方が結果がよい。
過酸化銀にカドミウム成分およびタリウムなど
のその他の成分を含有せしめるには、水酸化アル
カリと硝酸銀とを酸化剤の存在の下で反応させ
て、生成する過酸化銀を過乾燥前のスラリー中
にカドミウム成分およびその他の成分を添加混合
した後過乾燥すると都合がよいが、一旦乾燥し
た過酸化銀を分散媒中に再分散してカドミウムお
よびその他の成分を添加してもよいし、また過酸
化銀を乾燥状態のままこれにカドミウムおよびそ
の他の成分を機械的に混合してもよい。また別の
添加方法としてカドミウム成分およびその他の成
分を過酸化銀製造工程に使用する硝酸銀溶液、ア
ルカリ液、酸化剤、使用水中に混入させておいて
過酸化銀の生成反応を行なわせてもよい。
過酸化銀に含有させるカドミウム成分は金属と
して0.03重量%以上、テルル成分を過酸化銀中に
含有させる場合は金属として0.01重量%以上、タ
リウム、水銀成分を過酸化銀に含有させる場合ま
たは鉛、ゲルマニウム成分を電解液中に含有させ
ずに過酸化銀中に含有させる場合は前記カドミウ
ム及びテルル以外の成分の合計で0.01重量%以上
が必要である。これら添加成分の下限添加量であ
るカドミウム0.03重量%、テルル0.01重量%およ
びタリウムなどのその他の成分0.01重量%を組合
せて使用した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電池の安定性を著しく改善す
る。同等の安定性を求めるためにはカドミウムを
0.3重量%以上使用する必要があることから明ら
かにこれらの成分添加による相乗効果を示すもの
と考えられる。カドミウム、テルルおよびタリウ
ムなどのその他の元素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。
過酸化銀に添加するカドミウムおよびその他の
元素成分の使用量の上限は合計量で10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10重量%以上
の添加も可能で、この場合でも安定性が低下する
ことはない。またタリウムおよび水銀成分の添加
はこれぞれ3重量%をこえても効果の顕著性は認
められない。
使用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。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
CdTeO3,CdTeO4,Cd―Te合金粉末を添加する
こともできる。
使用するタリウム、鉛、ゲルマニウムおよび水
銀成分の形態は前記カドミウム、テルルと同様ど
んな形態でもよく、酸化物、金属、塩、金属間化
合物でもよい。
アルカリ電解液にテルル成分を添加する場合に
は0.01g/の添加で効果が認められるが、本格
的な効果を得るためには0.02g/以上、好まし
くは0.04g/以上添加するのがよい。またテル
ル成分の添加は濃度が大となると、つて効果が減
ずる現象が認められるが、5g/以下なら効果
が認められ、3g/以下が好ましく、過酸化銀
中のカドミウム成分が0.3重量%以下のときは1.0
g/以下が望ましい。
電解液に添加する鉛成分、ゲルマニウム成分は
それらの合計量で0.01g/の添加で効果が認め
られ、5g/以上ではもはやそれ以上の効果は
あまり望めない。電解液に添加するこれらの成分
はアルカリに可溶性であればその選択は自由であ
る。
以上述べたようにアルカリ電解液に可溶なテル
ル、鉛、ゲルマニウムの成分は過酸化銀に添加し
ても、電池中ではアルカリ電解液に可溶となるの
で、過酸化銀中に添加しなくても、アルカリ電解
液中に加えておけばほぼ同様な安定効果を示す。
したがつて、これらアルカリに可溶なテルル、
鉛、ゲルマニウム成分は過酸化銀中とアルカリ電
解液の両者に分けて添加することもできる。
以下この発明を実施例について説明する。
実施例 1
アルカリ液中で硝酸銀と過硫酸カリウムを用い
て合成した過酸化銀の乾燥物100gを1000mlの純
水中に投入し撹拌して分散させ、この中にカドミ
ウム源としてCdO、テルル源としてTeO2を、ま
た鉛、タリウム、ゲルマニウムおよび水銀源とし
てはそれぞれPbO、Tl2O3、GeO2、HgOを使用し
て、所定量を水分散液として加えて10分間撹拌後
過乾燥した。安定性試験には40重量%の水酸化
カリウム水溶液中で40℃、240時間当りのガス発
生率ならびに過酸化銀中の添加成分の含有率を測
定した。結果を第1表に示す。
This invention relates to improvements in silver peroxide batteries using silver peroxide as the main anode material. Conventional alkaline batteries have been known to use an active material based on silver peroxide for the anode and zinc, etc. for the cathode, but silver peroxide has a lower oxygen content than other oxides such as silver oxide. Since the content is large, the discharge performance of batteries using this material is significantly improved. However, silver peroxide has low stability within the battery and gradually decomposes into silver oxide and oxygen, so the oxygen generated during storage of the battery increases the internal pressure of the battery, causing expansion or deformation of the battery. In severe cases, it may even be destroyed. Such decomposition of silver peroxide (also called self-discharge) causes a decrease in the amount of effective silver peroxide, making it impossible to obtain the designed capacitance. This problem of self-discharge rate is particularly important for batteries with long lifespans. The reason for these drawbacks of silver peroxide batteries is thought to be due to the high activity of silver peroxide, which reacts with the alkaline electrolyte in contact with it. In order to eliminate this drawback, US Pat. No. 3,017,448 describes coating the surface of silver peroxide particles with silver lead acid, thereby improving the storage performance of the battery. As a result of various studies on stabilizing silver peroxide batteries, the inventors conducted a test in which various additives were added to the produced silver peroxide in order to stabilize the silver peroxide used as an anode active material. It was discovered that good stability was exhibited when a lead source and an aluminum source were simultaneously added to either the silver peroxide electrode or the alkaline electrolyte of a silver peroxide battery. Disclosed as No. 1984-84428. Subsequently, he discovered that stability could be dramatically improved by simultaneously adding a cadmium component to silver peroxide and a tellurium component to either silver peroxide or the alkaline electrolyte of a silver peroxide battery. No. 55-99418. The present invention is a further improvement of the invention relating to a silver peroxide battery to which a cadmium component and a tellurium component are added. The present invention was achieved by discovering that even better stability could be obtained. Accordingly, an object of the present invention is to provide a silver peroxide battery whose anode is formed using silver peroxide as a main ingredient, and whose stability is significantly improved. According to this invention, in the silver peroxide battery, in addition to containing 0.03% by weight or more of a cadmium component as a metal in silver peroxide as an essential component, and a tellurium component in at least one of the silver peroxide or the alkaline electrolyte, Furthermore, a silver peroxide battery is provided which contains at least one component selected from thallium, mercury, lead, and germanium as a selective component. Among these selected components, thallium and mercury are insoluble in alkali, so they are added to silver peroxide, and lead and germanium are soluble in alkali, so they are added to at least one of silver peroxide or the alkaline electrolyte. Just let it happen. The most preferable silver peroxide to be used is one produced by reacting an aqueous silver nitrate solution with an oxidizing agent such as potassium persulfate in an alkaline solution, but this invention is also applicable to silver peroxide produced by other production methods, such as electrolytic oxidation. However, silver peroxide manufactured by the former method has better results. To make silver peroxide contain cadmium components and other components such as thallium, alkali hydroxide and silver nitrate are reacted in the presence of an oxidizing agent, and the resulting silver peroxide is added to the slurry before overdrying. Although it is convenient to add and mix the cadmium component and other components and then over-dry it, it is also possible to re-disperse the dried silver peroxide in a dispersion medium and add cadmium and other components. Cadmium and other components may be mechanically mixed into the dry silver. Alternatively, the cadmium component and other components may be mixed into the silver nitrate solution, alkaline solution, oxidizing agent, and water used in the silver peroxide manufacturing process, and then the silver peroxide production reaction may occur. . Cadmium component to be included in silver peroxide is 0.03% by weight or more as a metal, if tellurium component is included in silver peroxide, 0.01% by weight or more as metal, thallium, mercury component is to be included in silver peroxide, or lead, When the germanium component is contained in silver peroxide without being contained in the electrolyte, the total amount of components other than cadmium and tellurium must be 0.01% by weight or more. Even when using a combination of the lower limit addition amounts of cadmium (0.03% by weight), tellurium (0.01%), and other components such as thallium (0.01% by weight), the stability of the battery is improved compared to conventional technology that uses cadmium alone. significantly improve. For equivalent stability, use cadmium.
Since it is necessary to use 0.3% by weight or more, it is considered that the addition of these components clearly shows a synergistic effect. Of course, when other elements such as cadmium, tellurium, and thallium are used together, the effect of reducing the amount of oxygen generated is sufficiently effective compared to samples without additives, but if the content of each element is below the above lower limit addition amount, the effect is less effective. The saliency of is insufficient. The upper limit of the amount of cadmium and other elemental components added to silver peroxide is preferably about 10% by weight in total; using an excessive amount will reduce the purity of silver peroxide and reduce the amount of electricity generated. will be invited. However, when used as an extender for forming a battery anode, it is possible to add 10% by weight or more, and even in this case, the stability will not decrease. Furthermore, no significant effect is observed even when the addition of thallium and mercury components exceeds 3% by weight. Examples of cadmium components used include cadmium oxide, cadmium hydroxide, metallic cadmium powder,
Examples include cadmium sulfide, cadmium sulfate, cadmium nitrate, cadmium stearate, cadmium formate, and cadmium selenide, which may be used alone or in combination. Examples of the tellurium component to be used include tellurium dioxide, tellurium trioxide, metallic tellurium powder, telluric acid, tellurite acid, or alkali salts thereof, and these can be used alone or in combination. Also compounds and alloys containing both cadmium and tellurium, e.g.
CdTeO 3 , CdTeO 4 , and Cd—Te alloy powders can also be added. The thallium, lead, germanium, and mercury components used may be in any form, similar to the above-mentioned cadmium and tellurium, and may be oxides, metals, salts, or intermetallic compounds. When adding a tellurium component to an alkaline electrolyte, an effect can be seen with addition of 0.01 g/, but in order to obtain a full-scale effect, it is recommended to add 0.02 g/or more, preferably 0.04 g/ or more. In addition, when the concentration of tellurium component is increased, it is observed that the effect decreases, but the effect is recognized when the concentration is 5 g/or less, and 3 g/or less is preferable, and the cadmium component in silver peroxide is 0.3% by weight or less. Time is 1.0
g/or less is desirable. The effect of the lead component and germanium component added to the electrolytic solution is recognized when the total amount thereof is 0.01 g/, and if it is 5 g/or more, no further effect can be expected. These components to be added to the electrolytic solution can be freely selected as long as they are soluble in alkali. As mentioned above, tellurium, lead, and germanium components that are soluble in alkaline electrolyte should not be added to silver peroxide because they become soluble in alkaline electrolyte in the battery even if they are added to silver peroxide. However, when added to an alkaline electrolyte, it exhibits almost the same stabilizing effect.
Therefore, these alkali-soluble tellurium,
The lead and germanium components can also be added separately to both the silver peroxide and the alkaline electrolyte. This invention will be described below with reference to embodiments. Example 1 100 g of dried silver peroxide synthesized using silver nitrate and potassium persulfate in an alkaline solution was poured into 1000 ml of pure water, stirred and dispersed, and CdO was added as a cadmium source and CdO was added as a tellurium source. TeO 2 and PbO, Tl 2 O 3 , GeO 2 , and HgO were used as lead, thallium, germanium, and mercury sources, respectively, and predetermined amounts were added as an aqueous dispersion, stirred for 10 minutes, and then overdried. In the stability test, the gas generation rate per 240 hours and the content of added components in silver peroxide were measured at 40°C in a 40% by weight aqueous potassium hydroxide solution. The results are shown in Table 1.
【表】【table】
【表】
試験No.1〜11の比較例中No.1〜No.7は添加成分
を全く含有しないが、1種類のみ含有するもので
あり、また試験No.8〜11はカドミウムとテルルの
両者のみを含有するものであつて、1種類のみの
含有ではガス発生率が250μ/g・240時間以下
のものは存在しない。試験No.12以下は本発明例を
示すものであつて、試験No.12〜15は本発明の添加
の下限値のものであるが試験No.11のカドミウムと
テルル添加のみのものに比してかなり改善された
値を示し、極めて微量の鉛、タリウム、ゲルマニ
ウム、水銀の添加でも相乗効果を示している。試
験No.16,17は試験No.9に鉛、タリウム等の添加成
分を0.05%、試験No.18〜22は試験No.8に0.10%程
度を加えることにより、カドミウムおよびテルル
の両者のみの添加の場合より著しく顕著にガス発
生率が低下している。試験No.23〜26はカドミウ
ム、テルルの他鉛、タリウムの含有量も多い場合
であるが、これら以上含有させてももはやこれ以
上の改善は期待できない結果を示している。
実施例 2
アルカリ液中で硝酸銀と過硫酸カリウムを用い
て過酸化銀を合成する反応において、原料である
硝酸銀液を弱硝酸酸性にしておき、この中に添加
剤であるカドミウムおよびテルルを酸化物として
添加し、またその他の添加成分であるタリウム、
鉛、ゲルマニウム、水銀のいずれかを酸化物の形
で添加溶解した後過酸化銀を製造した。実施例1
と同様にガス発生率を測定した。結果を第2表に
示す。[Table] Among the comparative examples of Test Nos. 1 to 11, No. 1 to No. 7 contain no additive components at all, but only one kind, and Test Nos. 8 to 11 contain cadmium and tellurium. There is no product that contains only one type and has a gas generation rate of 250 μ/g/240 hours or less. Test No. 12 and below show examples of the present invention, and Test No. 12 to 15 are at the lower limit of addition of the present invention, but compared to Test No. 11, which only added cadmium and tellurium. It shows a significantly improved value, and even the addition of extremely small amounts of lead, thallium, germanium, and mercury shows a synergistic effect. Test Nos. 16 and 17 added 0.05% of lead, thallium, and other additives to Test No. 9, and Tests No. 18 to 22 added about 0.10% to Test No. 8 to remove only cadmium and tellurium. The gas generation rate is significantly lower than in the case of addition. Test Nos. 23 to 26 involve large amounts of lead and thallium in addition to cadmium and tellurium, but the results show that no further improvement can be expected even if more than these are contained. Example 2 In a reaction to synthesize silver peroxide using silver nitrate and potassium persulfate in an alkaline solution, the raw material silver nitrate solution was made weakly acidic with nitric acid, and the additives cadmium and tellurium were added to the oxide. and other additive components such as thallium,
Silver peroxide was produced by adding and dissolving lead, germanium, or mercury in the form of oxides. Example 1
The gas generation rate was measured in the same manner. The results are shown in Table 2.
【表】
上表の結果から添加剤は過酸化銀が生成した後
に添加しても、その製造工程で予め加えておいて
も第1表の試験No.18〜21と対比してほぼ同様の成
積がえられることが判つた。
なお、この試験においてガス発生率測定のアル
カリ液として40%の水酸化ナトリウム水溶液を用
いて40℃、240時間の値を求めたが、上表とほぼ
類似の結果が得られた。
実施例 3
アルカリ液中で硝酸銀と過硫酸カリウムを用い
て合成した過酸化銀の乾燥物100gを1000mlの純
水中に投入し撹拌してよく分散させた。この中に
カドミウム源としてCdO、必要に応じてタリウ
ム源としてTl2O3を使用し、それぞれの所定量を
水分散液として加えて10分間撹拌後、過乾燥し
た。一方、電池の電解液に相当する40重量%の水
酸化カリウム水溶液に所定のテルル濃度を与える
ように二酸化テルルを加えかつ必要に応じて鉛、
ゲルマニウム源を酸化物の形で加え、この液中に
おける40℃での各添加成分含有の過酸化銀の240
時間当りのガス発生率を測定した。結果を第3表
に示す。[Table] From the results in the above table, whether the additive is added after silver peroxide is formed or added in advance during the manufacturing process, the results are almost the same compared to Test Nos. 18 to 21 in Table 1. It turned out that it was possible to make progress. In this test, a 40% aqueous sodium hydroxide solution was used as the alkaline solution for gas generation rate measurement, and values were obtained at 40°C for 240 hours, and results almost similar to those in the table above were obtained. Example 3 100 g of dried silver peroxide synthesized using silver nitrate and potassium persulfate in an alkaline solution was poured into 1000 ml of pure water and stirred to disperse it well. CdO was used as a cadmium source, and Tl 2 O 3 was used as a thallium source if necessary, and predetermined amounts of each were added as an aqueous dispersion, stirred for 10 minutes, and then overdried. On the other hand, tellurium dioxide was added to a 40% by weight aqueous potassium hydroxide solution, which corresponds to the battery electrolyte, to give a predetermined tellurium concentration, and if necessary, lead was added.
A germanium source is added in the form of an oxide, and the concentration of silver peroxide containing each additive component in this solution at 40°C is 240°C.
The gas generation rate per hour was measured. The results are shown in Table 3.
【表】【table】
【表】
上表の結果からアルカリに可溶のテルル、鉛、
ゲルマニウムは過酸化銀に含有させずアルカリ液
中に加えた場合も安定性において類似の効果を示
している。試験No.31〜38ではタリウムの併用によ
つてテルルの少量添加でも充分相乗効果が表われ
ている。しかし、この組合せに関しては試験No.36
のように過酸化銀中のカドミウムが0.3%と低い
ときは電解液中のテルルは1.0g/でも若干成
績が低下するようである。No.37,38はカドミウム
が1%以上となると、テルルは3.0g/でも支
障がなく、またNo.39,40ではテルルが5.0g/
でもよいが6.0g/では多すぎることを示して
いる。試験No.42〜45ではアルカリ電解液中に鉛ま
たはゲルマニウムを添加した結果でいずれも良好
な安定性を示している。[Table] From the results in the table above, the alkali-soluble tellurium, lead,
Similar effects on stability have been shown when germanium is added to an alkaline solution without being included in silver peroxide. In Test Nos. 31 to 38, sufficient synergistic effects were exhibited even with the addition of a small amount of tellurium when thallium was used in combination. However, regarding this combination, test No. 36
When the cadmium in the silver peroxide is as low as 0.3%, the performance seems to deteriorate slightly even if the tellurium in the electrolyte is 1.0g/. For No. 37 and 38, if cadmium is 1% or more, tellurium is 3.0 g/min without any problem, and for No. 39 and 40, tellurium is 5.0 g//
Although it is possible, 6.0g/ is shown to be too much. Test Nos. 42 to 45 showed good stability when lead or germanium was added to the alkaline electrolyte.
Claims (1)
銀電池において、過酸化銀にカドミウム成分を金
属として0.03重量%以上含有させ、テルル成分を
過酸化銀またはアルカリ電解液の少くとも一方に
含有させ、さらにタリウム、水銀、鉛およびゲル
マニウムから選ばれる少くとも1種の成分を含有
させたことから成り、その際タリウムおよび水銀
成分がそれぞれ単独または合計量で金属として
0.01重量%以上の量で過酸化銀に添加され、鉛お
よびゲルマニウム成分が過酸化銀またはアルカリ
電解液の少くとも一方に添加されていることを特
徴とする過酸化銀電池。 2 過酸化銀中に含有させるテルル成分が金属と
して0.01重量%以上である、特許請求の範囲第1
項に記載の過酸化銀電池。 3 過酸化銀中に含有させる鉛および(または)
ゲルマニウム成分がそれぞれ単独または合計で金
属として0.01重量%以上である、特許請求の範囲
第1項に記載の過酸化銀電池。[Scope of Claims] 1. In a silver peroxide battery in which the anode is formed using silver peroxide as a main ingredient, silver peroxide contains a cadmium component of 0.03% by weight or more as a metal, and a tellurium component is added to silver peroxide or an alkaline electrolyte. It consists of containing at least one component and further containing at least one component selected from thallium, mercury, lead and germanium, in which case thallium and mercury components are individually or in total amount as metals.
A silver peroxide battery, characterized in that lead and germanium components are added to silver peroxide in an amount of 0.01% by weight or more, and lead and germanium components are added to at least one of silver peroxide or an alkaline electrolyte. 2 Claim 1, wherein the tellurium component contained in silver peroxide is 0.01% by weight or more as a metal.
The silver peroxide battery described in section. 3. Lead and/or contained in silver peroxide
The silver peroxide battery according to claim 1, wherein each germanium component is contained individually or in total in an amount of 0.01% by weight or more as a metal.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55140400A JPS5765671A (en) | 1980-10-09 | 1980-10-09 | Silver peroxide battery |
| 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 |
|---|---|---|---|
| JP55140400A JPS5765671A (en) | 1980-10-09 | 1980-10-09 | Silver peroxide battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5765671A JPS5765671A (en) | 1982-04-21 |
| JPS6211459B2 true JPS6211459B2 (en) | 1987-03-12 |
Family
ID=15267895
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55140400A Granted JPS5765671A (en) | 1980-06-23 | 1980-10-09 | Silver peroxide battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5765671A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58152373A (en) * | 1982-03-05 | 1983-09-09 | Seiko Instr & Electronics Ltd | Silver peroxide cell |
| JPS5918575A (en) * | 1982-07-20 | 1984-01-30 | Seiko Electronic Components Ltd | Manufacture of silver peroxide battery |
| US20120164526A1 (en) * | 2009-03-27 | 2012-06-28 | Zpower, Llc | Cathode |
-
1980
- 1980-10-09 JP JP55140400A patent/JPS5765671A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5765671A (en) | 1982-04-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3111634B2 (en) | Manufacturing method of zinc alkaline battery | |
| JP3018715B2 (en) | Manufacturing method of zinc alkaline battery | |
| JPS58131660A (en) | Reducing agent in alkali battery electrolyte | |
| JPS6211459B2 (en) | ||
| 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 | |
| JPS6164076A (en) | Electrochemical battery | |
| JPS6090827A (en) | Permanganic acid process for manufacturing manganese dioxide from manganous salt | |
| JP2737233B2 (en) | Zinc alkaline battery | |
| JPS61153950A (en) | Zinc alkaline storage battery | |
| JPS605528B2 (en) | Method for producing silver peroxide | |
| JP2754864B2 (en) | Manufacturing method of zinc alkaline battery | |
| JPH0576745B2 (en) | ||
| JP2788530B2 (en) | Method for producing gelled negative electrode for alkaline dry battery and gelled negative electrode produced by the method | |
| JPH0317181B2 (en) | ||
| JP3178160B2 (en) | Method for producing negative electrode for button-type alkaline battery and button-type alkaline battery | |
| JPH0750612B2 (en) | Zinc alkaline battery | |
| JPS58225565A (en) | Alkaline battery | |
| JP2737232B2 (en) | Zinc alkaline battery | |
| JP2737231B2 (en) | Zinc alkaline battery | |
| JP2737230B2 (en) | Zinc alkaline battery | |
| JP2002373651A (en) | Alkaline battery | |
| JPS5920602B2 (en) | Production method of silver oxide for batteries | |
| JPS6177257A (en) | Zinc alkaline battery |