JPH0118546B2 - - Google Patents
Info
- Publication number
- JPH0118546B2 JPH0118546B2 JP56062872A JP6287281A JPH0118546B2 JP H0118546 B2 JPH0118546 B2 JP H0118546B2 JP 56062872 A JP56062872 A JP 56062872A JP 6287281 A JP6287281 A JP 6287281A JP H0118546 B2 JPH0118546 B2 JP H0118546B2
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- solution
- nickel salt
- filling
- immersed
- 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
- 238000000034 method Methods 0.000 claims description 18
- 150000002815 nickel Chemical class 0.000 claims description 11
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 claims description 10
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 8
- 239000012670 alkaline solution Substances 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 6
- 239000000758 substrate Substances 0.000 claims description 6
- 239000012266 salt solution Substances 0.000 claims description 4
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000006183 anode active material Substances 0.000 claims 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 238000007654 immersion Methods 0.000 description 7
- 238000005868 electrolysis reaction Methods 0.000 description 5
- 238000000197 pyrolysis Methods 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000011149 active material Substances 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 210000005069 ears Anatomy 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- UGKDIUIOSMUOAW-UHFFFAOYSA-N iron nickel Chemical compound [Fe].[Ni] UGKDIUIOSMUOAW-UHFFFAOYSA-N 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
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
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/32—Nickel oxide or hydroxide electrodes
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
アルカリ蓄電池の焼結式陽極板に於ける活物質
の充填方法には、ニツケル塩溶液を真空含浸後ア
ルカリ溶液中で電気分解を行う電気分解法、ニツ
ケル塩溶液に浸漬乾燥後、アルカリ溶液に浸漬し
て水酸化ニツケルとする化学含浸法等があるが、
いずれもいくつかの工程を組合せて繰り返し行う
ため多大の時間と工数とを要する欠点がある。又
ニツケル塩中に焼結多孔性基体を浸漬して陰電解
により水酸化物を析出させる電析充填法もある
が、電解のために多くの電気エネルギーを要する
とともに複雑な設備となるため量産化の設備投資
が大きくなる欠点があつた。これ等の方法と別に
焼結多孔性基板をニツケル塩に浸漬後水蒸気中で
加熱分解しニツケルの大部分を水酸化ニツケルと
する加熱分解方法があり、簡単な工程で安価に製
造し得る利点があるが、浸漬分解の工程をある程
度繰り返すとある限界値以上には充填できない欠
点がある。
本発明はこの熱分解充填法の改良に関するもの
である。熱分解充填法である限界値以上にニツケ
ル活物質を充填できないのは、分解による生成物
が水酸化ニツケルとニツケル塩との固溶体か混合
体であり、この未反応ニツケル塩の容積が活物質
となる水酸化ニツケルの容積よりも大であること
にある。
本発明はこの未反応ニツケル塩を浸漬熱分解を
繰り返す途中で、一旦NaOH又はKOH等のアル
カリ水溶液に浸漬してほぼ100%まで水酸化ニツ
ケルに変化させ、水洗乾燥によりアルカリ分を除
去することにより、ニツケル塩から水酸化ニツケ
ルへの変化に伴う充填物容積の縮少をうながし、
焼結多孔質体中に余有空隙を生ぜしめこの空隙に
再びニツケル塩の浸漬熱分解充填を繰り返して高
容量密度のアルカリ蓄電池用陽極板を得ることに
ある。別に熱分解生成物をアルカリ溶液中で充放
電を行つて水酸化ニツケル化を行う方法もある
が、多くの電気エネルギーを要すると共に工程が
それだけ複雑となり、単なる焼結多孔基体中の活
物質体の容積減少のためにはアルカリ溶液浸漬の
みで十分である。
本発明の実施例及び従来法による実験結果につ
いて次に述べる。
ペースト状ニツケル粉末を鉄ニツケルメツキ製
の多孔薄板に塗布し乾燥後焼結して得た多孔度約
80%、厚さ約1mmの多孔質焼結基板に集電用耳部
を残して縦横ともに100mmに切断し、この基板を
硝酸ニツケル水溶液に浸漬後予備乾燥して水蒸気
雰囲気中で加熱分解する工程を6回繰返した後、
濃度約20%のNaOH水溶液中に浸漬して水洗乾
燥し、再び前記熱分解充填を6回行い、その後濃
度約10%のNaOH中で別に準備したダミー極板
と組合せて化成して陽極板を作成した。
別に同一処方で同一寸法に製作したニツケル多
孔質基板を従来法により硝酸ニツケル水溶液に浸
漬予備乾燥後、加熱分解を12回繰返し同様に
NaOH中で化成を行い陽極板とした。前者をA
とし、後者をBとして比較すると、化成後の水酸
化ニツケルの充填密度は次表の通りとなつた。
Methods for filling active materials in sintered anode plates for alkaline storage batteries include electrolysis, which involves vacuum impregnation with a nickel salt solution and then electrolysis in an alkaline solution, and immersion in a nickel salt solution, drying, and then immersion in an alkaline solution. There are chemical impregnation methods that use nickel hydroxide.
Both methods have the drawback of requiring a large amount of time and man-hours because several steps are combined and repeated. There is also an electrodeposition filling method in which a sintered porous substrate is immersed in nickel salt and hydroxide is deposited by negative electrolysis, but mass production is difficult because electrolysis requires a lot of electrical energy and requires complicated equipment. The disadvantage was that the capital investment would be large. Apart from these methods, there is a thermal decomposition method in which a sintered porous substrate is immersed in nickel salt and then thermally decomposed in steam to convert most of the nickel into nickel hydroxide, which has the advantage of being manufactured at low cost through a simple process. However, there is a drawback that if the immersion decomposition process is repeated to a certain extent, it cannot be filled beyond a certain limit. The present invention relates to improvements in this pyrolytic filling method. The reason why the nickel active material cannot be filled above the limit value in the thermal decomposition filling method is that the product of decomposition is a solid solution or mixture of nickel hydroxide and nickel salt, and the volume of this unreacted nickel salt is larger than the active material. The reason is that the volume is larger than that of nickel hydroxide. In the present invention, this unreacted nickel salt is immersed in an alkaline aqueous solution such as NaOH or KOH during repeated immersion pyrolysis to convert it to almost 100% nickel hydroxide, and the alkali content is removed by washing with water and drying. , promotes a reduction in the filling volume due to the change from nickel salt to nickel hydroxide,
The purpose of the present invention is to create residual voids in the sintered porous body and repeat immersion pyrolysis filling of nickel salt into the voids to obtain a high capacity density anode plate for an alkaline storage battery. Another method is to charge and discharge the thermal decomposition product in an alkaline solution to convert it into nickel hydroxide, but this requires a lot of electrical energy and the process is complicated. Alkaline solution immersion alone is sufficient for volume reduction. Experimental results according to examples of the present invention and conventional methods will be described below. The porosity obtained by applying paste-like nickel powder to a porous thin plate made of iron nickel metal and sintering it after drying.
A process of cutting a porous sintered substrate with a thickness of 80% and approximately 1 mm into 100 mm pieces both vertically and horizontally, leaving current collecting ears, and immersing this substrate in an aqueous nickel nitrate solution, pre-drying it, and thermally decomposing it in a steam atmosphere. After repeating 6 times,
It was immersed in a NaOH aqueous solution with a concentration of about 20%, washed with water, and dried, and then subjected to the above-described pyrolysis filling six times, and then combined with a separately prepared dummy electrode plate in NaOH with a concentration of about 10% and chemically formed to form an anode plate. Created. A nickel porous substrate made with the same recipe and the same dimensions was immersed in a nickel nitrate aqueous solution using the conventional method, pre-dried, and then thermally decomposed 12 times in the same manner.
It was formed into an anode plate in NaOH. A for the former
When compared with the latter as B, the packing density of nickel hydroxide after chemical formation was as shown in the following table.
【表】
このA及びBの陽極板を夫々別に準備した両試
料より大容量のカドミウム陰極板とセパレータを
介して組合せ、合成樹脂製の容器に入れ比重1.20
(20℃換算)のKOH水溶液を電解液として注入し
0.8Aの電流で20時間充電し、その後約1時間静
置した後同じく0.8Aの電流で放電を行つた。こ
の充放電中の外気温は20〜25℃とした。その結果
A、B両者の1.0V迄の放電持続時間は図に示す
通り、Aは5時間40分で4.53Ah、Bは4時間31
分で3.61Ahであつた。
また本実験では熱分解充填を6回繰り返した
後、アルカリ溶液に浸漬水洗乾燥の工程を行い、
その後さらに6回熱分解充填を繰り返し行つた
が、別の実験で従来通り12回熱分解充填を行つた
後アルカリ溶液に浸漬乾燥し、さらに3回熱分解
充填を行つた結果、水酸化ニツケルとしてほぼ同
様の充填密度が得られ、同条件での化成後の放電
容量は4.45Ahであつた。
このように本発明は簡便な方法でしかも電気分
解法等と同等かそれ以上の高容量密度の陽極板が
得られる優れた製造方法である。[Table] The anode plates of A and B were combined with a cadmium cathode plate with a larger capacity than both samples prepared separately via a separator, and placed in a synthetic resin container with a specific gravity of 1.20.
Inject a KOH aqueous solution (calculated at 20℃) as an electrolyte.
The battery was charged with a current of 0.8A for 20 hours, then left to stand for about 1 hour, and then discharged with a current of 0.8A. The outside temperature during this charging and discharging was 20 to 25°C. As a result, the discharge duration to 1.0V for both A and B is 4.53Ah in 5 hours and 40 minutes for A and 4.53Ah for B in 4 hours and 31 minutes, as shown in the figure.
It was 3.61Ah per minute. In addition, in this experiment, after repeating pyrolysis filling six times, a process of immersion in an alkaline solution, washing with water, and drying was performed.
After that, pyrolytic filling was repeated 6 more times, but in another experiment, pyrolytic filling was performed 12 times as before, then immersed in an alkaline solution and dried, and pyrolytic filling was performed 3 more times, resulting in nickel hydroxide. Almost the same packing density was obtained, and the discharge capacity after formation under the same conditions was 4.45 Ah. As described above, the present invention is a simple method and is an excellent manufacturing method that can produce an anode plate with a high capacity density equivalent to or higher than that of electrolysis or the like.
図は本発明による陽極板と従来の熱分解法によ
る陽極板の放電特性曲線を示す。
The figure shows the discharge characteristic curves of the anode plate according to the present invention and the anode plate prepared by the conventional pyrolysis method.
Claims (1)
体をニツケル塩溶液に浸漬し、次いで水蒸気雰囲
気中で加熱分解を行なつて水酸化ニツケルとする
工程を繰り返す陽極活物質充填法に於て、所定回
数の中間でアルカリ溶液に浸漬して水洗乾燥さ
せ、再びニツケル塩溶液に浸漬、加熱分解を繰返
し行つた後アルカリ水溶液中で充放電を行なうこ
とを特徴とするアルカリ蓄電池用陽極板の製造方
法。1 In an anode active material filling method in which a sintered porous metal substrate mainly composed of nickel powder is immersed in a nickel salt solution, and then thermally decomposed in a steam atmosphere to form nickel hydroxide, the process is repeated. A method for producing an anode plate for an alkaline storage battery, which comprises immersing it in an alkaline solution, washing and drying it with water, immersing it again in a nickel salt solution, repeating thermal decomposition, and then charging and discharging in an aqueous alkaline solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56062872A JPS57180075A (en) | 1981-04-24 | 1981-04-24 | Manufacture of positive plate for alkaline storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56062872A JPS57180075A (en) | 1981-04-24 | 1981-04-24 | Manufacture of positive plate for alkaline storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57180075A JPS57180075A (en) | 1982-11-05 |
| JPH0118546B2 true JPH0118546B2 (en) | 1989-04-06 |
Family
ID=13212790
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56062872A Granted JPS57180075A (en) | 1981-04-24 | 1981-04-24 | Manufacture of positive plate for alkaline storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57180075A (en) |
-
1981
- 1981-04-24 JP JP56062872A patent/JPS57180075A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57180075A (en) | 1982-11-05 |
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