JPS5924495B2 - Manufacturing method of silver oxide positive electrode - Google Patents
Manufacturing method of silver oxide positive electrodeInfo
- Publication number
- JPS5924495B2 JPS5924495B2 JP13933476A JP13933476A JPS5924495B2 JP S5924495 B2 JPS5924495 B2 JP S5924495B2 JP 13933476 A JP13933476 A JP 13933476A JP 13933476 A JP13933476 A JP 13933476A JP S5924495 B2 JPS5924495 B2 JP S5924495B2
- Authority
- JP
- Japan
- Prior art keywords
- silver oxide
- silver
- positive electrode
- manufacturing
- oxide positive
- 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
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 title claims description 22
- 229910001923 silver oxide Inorganic materials 0.000 title claims description 11
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 8
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 7
- 239000012670 alkaline solution Substances 0.000 claims description 6
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 4
- 238000006056 electrooxidation reaction Methods 0.000 claims description 3
- 239000007800 oxidant agent Substances 0.000 claims description 3
- GGCZERPQGJTIQP-UHFFFAOYSA-N sodium;9,10-dioxoanthracene-2-sulfonic acid Chemical compound [Na+].C1=CC=C2C(=O)C3=CC(S(=O)(=O)O)=CC=C3C(=O)C2=C1 GGCZERPQGJTIQP-UHFFFAOYSA-N 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 8
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 239000012153 distilled water Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000007774 positive electrode material Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 3
- 229910001961 silver nitrate Inorganic materials 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- DUCFBDUJLLKKPR-UHFFFAOYSA-N [O--].[Zn++].[Ag+] Chemical compound [O--].[Zn++].[Ag+] DUCFBDUJLLKKPR-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000007773 negative electrode material Substances 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
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AgOを正極活物質とし、例えば亜
鉛を負極活物質とするアルカリ電池の正極の改良に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in the positive electrode of an alkaline battery using silver divalent oxide AgO as a positive electrode active material and, for example, zinc as a negative electrode active material.
小形電子機器用の電源として、より高容量化の電池が指
向されているが、その中でも二価酸化銀を正極活物質と
する酸化銀−亜鉛系電池は、電池性能的にも、又高容量
化と言う点でも特にすぐれた電池である。Batteries with higher capacity are being sought as power sources for small electronic devices, and among these, silver-zinc oxide batteries, which use divalent silver oxide as the positive electrode active material, have excellent battery performance and high capacity. It is also a particularly excellent battery in terms of compatibility.
現在使用されている一価酸化銀A920と比較すると、
A9Oは、単位重量当たり1.86倍、容積当たり1.
93倍とエネルギー密度が大きい。しかし電池正極活物
質とする場合問題もある。その問題点は、AgOがアル
カリ溶液中で不安定であり、2Ag0→AI2O+XO
、様に分解反応が進み、安定なA920に変化すると同
時に酸素ガスを放出することである。従つて密閉電池を
構成した時、電池の内圧が上がり最終的には電池の膨張
、漏液等につながり、A90の特徴である高エネルギー
密度を活用することができない。又、AgOの性質とし
て、熱的に大変不安定であり、100℃近傍においても
上記分解反応が相当な速度で起こり、酸化銀及びA9O
(5Ag2Oの中間組成を有する銀酸化物ができる。こ
のため、化学酸化法、電気化学的酸化法等の湿式製法で
は、最終過程で生成、UOの乾燥を行わねばならないが
、高温での乾燥ができない為非常に長時間を要する欠点
がある。そこでメチルアルコール、エチルアルコールを
乾燥直前に用いることも考えられるが、A90が非常に
強力な酸化剤であるため、アルコールが還元剤として働
き、A90がA92Oに変化する。Compared to the currently used monovalent silver oxide A920,
A9O is 1.86 times more powerful per unit weight and 1.86 times more powerful per unit weight.
The energy density is 93 times higher. However, there are problems when using it as a battery positive electrode active material. The problem is that AgO is unstable in alkaline solution, and 2Ag0→AI2O+XO
As the decomposition reaction progresses, it changes to stable A920 and at the same time releases oxygen gas. Therefore, when a sealed battery is constructed, the internal pressure of the battery increases, which ultimately leads to expansion of the battery, leakage, etc., and the high energy density characteristic of A90 cannot be utilized. In addition, the nature of AgO is that it is very unstable thermally, and the above decomposition reaction occurs at a considerable rate even at around 100°C, resulting in silver oxide and A9O.
(A silver oxide with an intermediate composition of 5Ag2O is produced. Therefore, in wet manufacturing methods such as chemical oxidation method and electrochemical oxidation method, it is necessary to dry the UO produced in the final process, but drying at high temperature is not possible. Therefore, it is possible to use methyl alcohol or ethyl alcohol just before drying, but since A90 is a very strong oxidizing agent, the alcohol acts as a reducing agent and the A90 Changes to A92O.
又酸化に対して安定なアセトンでも若干のA90の生成
はまぬがれない。本発明者らは、銀塩もしくは銀粉をア
ルカリ水溶液中において、過硫酸カリウム、過マンガン
酸カリウム、次亜塩素塩等の酸化剤により酸化するか、
銀塩の水溶液又は銀粉の成形体を電気化学的酸化により
A90を得る方法において、得られたAgOをテトラヒ
ドロフランで処理することにより、アルカリ溶液中にお
けるガス発生速度を著しく抑制しうることを見出した。Furthermore, even with acetone which is stable against oxidation, some amount of A90 is inevitably generated. The present inventors oxidize silver salt or silver powder in an alkaline aqueous solution with an oxidizing agent such as potassium persulfate, potassium permanganate, or hypochlorite, or
In a method for obtaining A90 by electrochemical oxidation of an aqueous solution of a silver salt or a molded body of silver powder, it has been found that by treating the obtained AgO with tetrahydrofuran, the rate of gas generation in an alkaline solution can be significantly suppressed.
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.
蒸留水1tにか性ソーダ729を溶解したアルカリ溶液
を温度85℃に保ち、その溶液に過硫酸カリウム759
に若干の蒸留水を加えぺースト状としたものを加え終わ
ると同時に、100m1の蒸留水に硝酸銀Af!NO3
5l9を溶解した溶液を約10分間で滴下し、次に温度
90℃に上げ20分間反応させる。An alkaline solution of caustic soda 729 dissolved in 1 ton of distilled water is maintained at a temperature of 85°C, and potassium persulfate 759 is added to the solution.
At the same time as adding some distilled water to make a paste, add silver nitrate Af! to 100ml of distilled water! NO3
A solution in which 5l9 was dissolved was added dropwise over about 10 minutes, and then the temperature was raised to 90°C and the reaction was allowed to proceed for 20 minutes.
その間反応溶液は一定速度で攪拌する。反応終了後、溶
液中に生成しているAjOを沈降させて上澄液を捨て、
新たに蒸留水約1tを加え5分間攪拌し再度上澄液を捨
てる。この操作を繰り返し、上澄液のPHが9.5にな
るまで洗浄し、最終洗浄液をろ過しA9Oを得る。銀粉
末からMOを得る場合は、硝酸銀の代わりに銀粉末を加
えるか、銀粉末を成形体とし、それを電極としてアルカ
リ溶液中で陽極酸化すればよく、その後、蒸留水にて洗
浄しアルカリ分を除く。次に上記のようにアルカリ溶液
中において硝酸銀を過硫酸カリウムで酸化して得たAf
!Oを、水が付着したままの状態で各種有機溶剤に浸漬
して撹拌した後、温度30℃、−7601!I!lの減
圧下で乾燥し、゛随量になる迄の時間を求めた。Meanwhile, the reaction solution is stirred at a constant speed. After the reaction is complete, the AjO produced in the solution is precipitated and the supernatant liquid is discarded.
Add approximately 1 ton of distilled water, stir for 5 minutes, and discard the supernatant liquid again. This operation is repeated until the pH of the supernatant liquid reaches 9.5, and the final washing liquid is filtered to obtain A9O. When obtaining MO from silver powder, it is sufficient to add silver powder instead of silver nitrate, or to form a molded body of silver powder and anodize it in an alkaline solution using it as an electrode.Then, it is necessary to wash it with distilled water and remove the alkali solution. except for. Next, Af obtained by oxidizing silver nitrate with potassium persulfate in an alkaline solution as described above.
! After immersing O in various organic solvents with water still attached and stirring, the temperature was 30°C and -7601! I! It was dried under a reduced pressure of 1 liter, and the time required for it to reach its desired mass was determined.
同時にこの乾燥後のA9Oを温度70℃の10NK0H
水溶液中に4時間浸漬したときの平均ガス発生速度を測
定した。これらの結果を次表に示す。上記の結果より明
らかな様に有機溶剤にてA9Oを処理するとガス発生速
度は全般的に少なくなるが、エチルアルコールで処理し
た場合は、先にも述べた様に2価酸化銀の酸化銀化が進
み、その結果としてガス発生速度が見掛上減つている。
又、アセトンでは若干の酸化銀A92O化が進んだ結果
、ガス発生速度も若干減つたにすぎない。それに対しテ
トラヒドロフランで処理したものはAf!0の状態変化
はないにもかかわらずガス発生抑制効果が認められる。
なおこのガス発生抑制の効果は、A9Oを乾燥後にテト
ラヒドロフランで処理した場合も同様であつた。At the same time, this dried A9O was heated to 10NK0H at a temperature of 70°C.
The average gas generation rate was measured when immersed in an aqueous solution for 4 hours. These results are shown in the table below. As is clear from the above results, when A9O is treated with an organic solvent, the gas generation rate is generally reduced, but when treated with ethyl alcohol, as mentioned above, divalent silver oxide is converted to silver oxide. has increased, and as a result, the gas generation rate has apparently decreased.
Furthermore, in the case of acetone, the rate of gas generation was only slightly reduced as a result of the silver oxide A92O formation progressing to some extent. On the other hand, those treated with tetrahydrofuran had Af! Although there is no change in the zero state, the gas generation suppressing effect is observed.
The effect of suppressing gas generation was the same when A9O was dried and then treated with tetrahydrofuran.
以上のように本発明によれば、ガス発生の少ないA9O
を得ることができ、MOを正極活物質とする密閉電池を
可能にするものである。As described above, according to the present invention, A9O with less gas generation
This enables a sealed battery using MO as the positive electrode active material.
Claims (1)
、酸化剤又は電気化学的酸化により二価酸化銀を得る工
程と、この酸化銀をテトラヒドロフランにより処理する
工程とを有することを特徴とする酸化銀正極の製造法。1. A silver oxide positive electrode comprising a step of obtaining divalent silver oxide by oxidizing a silver salt or silver powder in an aqueous alkaline solution using an oxidizing agent or electrochemical oxidation, and a step of treating this silver oxide with tetrahydrofuran. manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13933476A JPS5924495B2 (en) | 1976-11-18 | 1976-11-18 | Manufacturing method of silver oxide positive electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13933476A JPS5924495B2 (en) | 1976-11-18 | 1976-11-18 | Manufacturing method of silver oxide positive electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53127644A JPS53127644A (en) | 1978-11-08 |
| JPS5924495B2 true JPS5924495B2 (en) | 1984-06-09 |
Family
ID=15242892
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13933476A Expired JPS5924495B2 (en) | 1976-11-18 | 1976-11-18 | Manufacturing method of silver oxide positive electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5924495B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05116734A (en) * | 1991-10-25 | 1993-05-14 | Daiwa Kenki Kk | Screw conveyor device |
-
1976
- 1976-11-18 JP JP13933476A patent/JPS5924495B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05116734A (en) * | 1991-10-25 | 1993-05-14 | Daiwa Kenki Kk | Screw conveyor device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53127644A (en) | 1978-11-08 |
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