JPS6074262A - Manufacture of nickel electrode - Google Patents
Manufacture of nickel electrodeInfo
- Publication number
- JPS6074262A JPS6074262A JP58180752A JP18075283A JPS6074262A JP S6074262 A JPS6074262 A JP S6074262A JP 58180752 A JP58180752 A JP 58180752A JP 18075283 A JP18075283 A JP 18075283A JP S6074262 A JPS6074262 A JP S6074262A
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- solution
- nickel nitrate
- substrate
- caustic soda
- 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.)
- Pending
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
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/26—Processes of manufacture
- H01M4/28—Precipitating active material on the carrier
-
- 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
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はアルカリ蓄電池に使用されるニッケル電極の改
良された製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved method of manufacturing nickel electrodes used in alkaline storage batteries.
ニッケル電極は水酸化ニッケルを活物質化とするもので
あり、従来からニッケル粉焼結体から々る多孔性ニッケ
ル基板を硝酸ニッケルの水溶液又は硝酸ニッケルの有機
溶液(メタノール溶液あるいはエタノール溶液等)へ浸
漬して硝酸ニッケルを該基板中に含浸せしめ、次いで、
この基板を苛性ソーダ溶液中に浸浴して基板中に含浸し
た硝酸ニッケルを水酸イヒニッケルとして活物質化する
方法で製造さ′i′1ていた。従って、かがる方法にお
いては、含浸−熱処理一活物質化一水洗一乾燥からなる
工程が含浸の]ザイクルとなっているが、かかる従来法
による94合にはI−リイクルで二ソクル基板中へ活物
質を十分充填することができず、/」2なくとも8〜1
0サイクルを繰り返す必要があり、サイクル数が多く、
製造に時間、労力を費すものとなっていた。このため、
硝酸ニラクル溶液の代替としてTit’i酸ニッケル溶
融塩を使用する方法も案出されているが、サイクル数の
低減vJできず、十分な効果が得らねるものではなかっ
た。心らに、ときの実容聞゛との百分率)は90〜95
%であるため、ニッケルの有効利用の点からは低いもの
となっていた。Nickel electrodes use nickel hydroxide as the active material, and conventionally, a porous nickel substrate made from sintered nickel powder is placed in an aqueous solution of nickel nitrate or an organic solution of nickel nitrate (methanol solution, ethanol solution, etc.). immersion to impregnate nickel nitrate into the substrate, and then
The substrate was manufactured by dipping the substrate in a caustic soda solution and converting the nickel nitrate impregnated into the substrate into an active material as nickel hydroxide. Therefore, in the darning method, the process consisting of impregnation, heat treatment, formation of active material, washing, and drying is the cycle of impregnation. The active material cannot be sufficiently filled into /'2 at least 8 to 1.
It is necessary to repeat the 0 cycle, and the number of cycles is large.
It was time-consuming and labor-intensive to manufacture. For this reason,
A method of using a molten nickel Tit'i acid salt as a substitute for the Niracle nitrate solution has been devised, but it has not been possible to reduce the number of cycles vJ and a sufficient effect has not been obtained. To the heart, the actual situation (percentage) is 90-95.
%, it was low from the point of view of effective use of nickel.
本発明はこのような従来の方法の欠点を改善すべく寿さ
れたものであり、硝酸ニッ〃ルの含浸条件と苛性ソーダ
による活物質化条件とを特定の・7・n四に選定するこ
とにより、サイクル数の低減及び利用率の向上の双方を
可能としたものである。The present invention has been developed in order to improve the drawbacks of the conventional method, and by selecting the conditions for impregnating nitrate with nitrate and the conditions for forming the active material with caustic soda to a specific value of 7.n4. , it is possible to both reduce the number of cycles and improve the utilization rate.
すガわち、本発明は、多孔性ニッケル基板を硝酸ニッケ
ル溶液中に浸漬して該基板に硝酸ニッケルを含浸せしめ
、次いで苛性ソーダ溶液中で前記硝酸ニッケル全水酸化
ニッケルとして活物質化せしめる方法において、前記硝
酸ニッケル溶液での含浸条件が温度65〜85℃及び比
重1.65〜1゜75であシ、前記苛性ソーダ溶液での
活物質化条件が比重1251以上であることを特徴とす
るものである。Specifically, the present invention provides a method in which a porous nickel substrate is immersed in a nickel nitrate solution to impregnate the substrate with nickel nitrate, and then the nickel nitrate is made into an active material as total nickel hydroxide in a caustic soda solution. , characterized in that the conditions for impregnation with the nickel nitrate solution are a temperature of 65 to 85°C and a specific gravity of 1.65 to 1°75, and the conditions for forming the active material in the caustic soda solution are a specific gravity of 1251 or more. be.
本発明における多孔性ニッケル基板は従来法と同様にニ
ッケル粉を焼結して得らノするニッケル粉焼結体が使用
され、このニッケル粉焼結体からなる基板は硝酸ニッケ
ル溶液に浸漬されて硝酸ニッケルが該基板中に含浸せし
められる。ここで、硝酸ニッケル溶液は硝酸ニッケルの
水溶液又は硝酸ニッケルをメタノール、エタノール等に
溶解した有機溶液を使用することができるが、本発明に
おいて、この溶液は温度が65〜85℃でしかも比重、
が165〜175であることを要する。溶液の温度が6
5℃以下の場合にd液粘性が増加してニッケル基板の細
孔部に寸で溶液が達せず、細孔部での含浸率が低下する
一方、85℃以上ではニッケル基板の腐食が大きく特性
が劣化するためである。又1、比TR1,65JJ下の
薄い溶液では一回の浸漬で含浸される硝酸ニッケルの累
′が少なく、一方、比重175以−ヒでは溶液の粘性が
増シ2、前述と同様にニッケル基板の細孔部に寸で達し
ない/こめでを)る。従って、含浸に使用される硝酸エ
タノールの量に1、上記条件に適合するよう、適宜(h
i、l整さ第1る。The porous nickel substrate in the present invention uses a nickel powder sintered body obtained by sintering nickel powder as in the conventional method, and the substrate made of this nickel powder sintered body is immersed in a nickel nitrate solution. Nickel nitrate is impregnated into the substrate. Here, as the nickel nitrate solution, an aqueous solution of nickel nitrate or an organic solution in which nickel nitrate is dissolved in methanol, ethanol, etc. can be used, but in the present invention, this solution has a temperature of 65 to 85°C, a specific gravity,
is required to be between 165 and 175. The temperature of the solution is 6
When the temperature is below 5℃, the viscosity of the d-liquid increases and the solution does not reach the pores of the nickel substrate, resulting in a decrease in the impregnation rate at the pores.On the other hand, when the temperature is above 85℃, the corrosion of the nickel substrate increases and the characteristics This is because it deteriorates. 1. In a thin solution with a specific gravity of 1,65 JJ or less, the amount of nickel nitrate impregnated in one immersion is small; on the other hand, with a specific gravity of 175 or more, the viscosity of the solution increases. It does not reach the pores of the body. Therefore, add 1 to the amount of nitric ethanol used for impregnation, and adjust accordingly (h) to meet the above conditions.
i, l order first.
このようにして、硝酸ニッケルがニッケルり占4反に含
浸した後は所定の熱処理後、苛性ソーダ溶液中に浸漬さ
れて活物質化処理が行なわれる。この浸ffにより、含
浸した硝酸ニッケルは水11夕化ニッケルに変化して、
ニッケル11う:極としての!苛性が刊与さ:l′t−
7りが、ここで使用され7る苛性ノーダ溶’ll’t
k、i比重1.25以上であることが必要である。この
俤・件で行なった場合には、析出する水酸化ニッケルの
密度が高く、次の充填の為の孔が十分に用意されて、基
板の細孔部に深く入るためと思われる。After the nickel oxide film is impregnated with nickel nitrate in this manner, it is subjected to a prescribed heat treatment and then immersed in a caustic soda solution to undergo an active material treatment. Through this immersion ff, the impregnated nickel nitrate changes to water 11 nickel,
Nickel 11: As a pole! Caustic is published: l't-
The caustic nodal solution used here is
It is necessary that the k and i specific gravity be 1.25 or more. This seems to be because when the process is carried out in this manner, the density of the precipitated nickel hydroxide is high, sufficient pores are prepared for the next filling, and the nickel hydroxide penetrates deeply into the pores of the substrate.
すなわち、第1図(イ)に示すように、上記条件で行々
つだ場合には、活物質1である水酸化ニッケルと導電材
であるニッケル粉2との接触面積が、同図(ロ)で示す
従来法によるものに比べで大きくなる/こめであり、こ
ノ1により、利用率も向上する。In other words, as shown in Figure 1 (A), if the above conditions are followed, the contact area between nickel hydroxide, which is the active material 1, and nickel powder 2, which is the conductive material, will be as shown in Figure 1 (A). ) is larger than that of the conventional method, and this method also improves the utilization rate.
卯、2図d含浸条件と活物質化条件とを夫々異ならしめ
て製造した場合の各含浸サイクル数に対する水酸化ニッ
ケルの含浸量をプロンi−した充lA特性を示すもので
あり、Aは硝酸ニッケル溶液の比mW、 1.609温
度60℃でかつ苛性ソーダ溶液の比重1.30の場合、
Bは硝酸ニッケル溶液の凡用1゜75、温度60℃でか
つ苛性ソーダ溶液の比重1゜20の場合、Cは硝酸ニッ
ケル溶液の比重1.75゜温度70℃でかつ苛性ソーダ
溶液の比7H〔1,20の場合、Dは7iFj酸ニツケ
ル溶液の比31i、 1.、75 v温度60℃でかつ
苛性ソーダ溶液■比*J、、3oの場合を示す。同図か
ら本発明の条件以外の場合にdlいずれもサイクル数の
低減がでキ力いことが認められる。Figure 2 d shows the full A characteristics of the impregnated amount of nickel hydroxide for each number of impregnation cycles when manufactured under different impregnation conditions and active material forming conditions, where A is nickel nitrate. The specific mW of the solution is 1.609.When the temperature is 60°C and the specific gravity of the caustic soda solution is 1.30,
If B is the general purpose of the nickel nitrate solution, 1°75, the temperature is 60°C, and the specific gravity of the caustic soda solution is 1°20, C is the specific gravity of the nickel nitrate solution, 1.75°, the temperature is 70°C, and the ratio of the caustic soda solution is 7H [1]. , 20, D is the ratio of 7iFj nickel acid solution 31i, 1. , 75 V, the temperature is 60° C., and the ratio of the caustic soda solution is *J, , 3o. From the same figure, it is recognized that under conditions other than the conditions of the present invention, the number of cycles can be reduced in both cases of dl.
一方、本発明方法により製造さt]たニッケル11−j
極は利用率が約100%であり、従来法に比べ高いもの
となり、又、サイクル数も4〜5回に低減せしめること
が可能となる。On the other hand, nickel 11-j produced by the method of the present invention
The utilization rate of the pole is approximately 100%, which is higher than that of the conventional method, and the number of cycles can be reduced to 4 to 5 times.
次に本発明を実施例に基づいて説、明する。Next, the present invention will be described and explained based on examples.
多孔度80チのニッケル粉焼結体からなる多孔性ニッケ
ル基板を比重1,72及び温度75℃の硝酸ニッケル溶
液に、40分浸漬し、次いで、比重13゜温度80℃の
苛性ソーダ溶液に浸漬した。かかる工程を1ザイクルと
し、各サイクル終了点での水酸化ニッケル含浸量1をプ
ロットし″′C第31閾e)曲線Eがイqらhた。この
曲I%!Fjは5ザイクル終了時点で仕上は品とし、次
いで、%Cで16時間充Tii’、 1.、、KCで放
市ルたところ、利用率は100チであ−)だ。第3図の
曲線Fは従来の方法によって製造されたものを示してお
り、この方法によって得られた極板全上記と同様にして
利用率全測定したところ、利用率は92%であった。A porous nickel substrate made of sintered nickel powder with a porosity of 80 cm was immersed in a nickel nitrate solution with a specific gravity of 1.72 and a temperature of 75°C for 40 minutes, and then in a caustic soda solution with a specific gravity of 13° and a temperature of 80°C. . This process is considered to be one cycle, and the amount of nickel hydroxide impregnated 1 at the end of each cycle is plotted, and the 31st threshold e) curve E is obtained.This song I%!Fj is at the end of 5 cycles. The finish was made good with %C, and then the product was charged for 16 hours with %C Tii', 1., KC, and the utilization rate was 100chi.).Curve F in Figure 3 shows the conventional method. When the utilization rate of all the electrode plates obtained by this method was measured in the same manner as above, the utilization rate was 92%.
以上のことから、本発明によって製造した場合には、サ
イクル数を低減せしめ、て製造時間、労力の軽減が可能
となるばかりでなく、利用率も]00係とカリ、その向
上が可能とガる。From the above, when manufacturing according to the present invention, it is possible to not only reduce the number of cycles and reduce manufacturing time and labor, but also to improve the utilization rate and potency. Ru.
第1図げ)、(ロ)はニッケル基板の含浸状態を示−1
−断面図11第2Iン1及び第3図C」−ライフル数に
対する水酸化ニッケル含浸量をプロットした充填時15
トヅ]である。
特許山数(1人 古河電池株式会社
代理人 弁理土佐 藤 莢 昭
第1図
(イ) (0)
第3図
電
フイクI峨
第2図
含
浸・
■
N1(oi
μ・
サイクI1./敬−Figure 1) and (b) show the impregnated state of the nickel substrate.
- Sectional view 11 2nd In 1 and 3rd C'' - At the time of filling 15 plotting the amount of nickel hydroxide impregnated against the number of rifles
Tozu]. Number of patents (1 person, agent for Furukawa Battery Co., Ltd., patent attorney Tosa Fuji) (0)
Claims (1)
〜175の硝酸ニッケル溶液中に浸漬して診基板中に硝
酸ニッケルを含浸せしめ、次いで比重1.25以上の苛
性ソーダ溶液中で前記硝酸ニッケルを水酸化ニッケルと
して活物質化せしめる仁と全性徴とするニッケル電極の
製造法。Porous nickel substrate at temperature 65-85℃, specific gravity 1.65
The diagnostic substrate is impregnated with nickel nitrate by immersing it in a nickel nitrate solution with a concentration of ~175, and then the nickel nitrate is converted into nickel hydroxide into an active material in a caustic soda solution with a specific gravity of 1.25 or more. Method for manufacturing nickel electrodes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58180752A JPS6074262A (en) | 1983-09-30 | 1983-09-30 | Manufacture of nickel electrode |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58180752A JPS6074262A (en) | 1983-09-30 | 1983-09-30 | Manufacture of nickel electrode |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6074262A true JPS6074262A (en) | 1985-04-26 |
Family
ID=16088693
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58180752A Pending JPS6074262A (en) | 1983-09-30 | 1983-09-30 | Manufacture of nickel electrode |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6074262A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62105370A (en) * | 1985-10-31 | 1987-05-15 | Shin Kobe Electric Mach Co Ltd | Manufacture of cathode plate for alkaline storage battery |
JPS63105468A (en) * | 1986-10-20 | 1988-05-10 | Sanyo Electric Co Ltd | Manufacture of nickel hydroxide electrode for alkaline storage battery |
JPS63314763A (en) * | 1987-06-17 | 1988-12-22 | Sanyo Electric Co Ltd | Manufacture of nickel hydroxide electrode for alkaline storage battery |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56149769A (en) * | 1980-04-21 | 1981-11-19 | Matsushita Electric Ind Co Ltd | Manufacture of electrode for battery |
-
1983
- 1983-09-30 JP JP58180752A patent/JPS6074262A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56149769A (en) * | 1980-04-21 | 1981-11-19 | Matsushita Electric Ind Co Ltd | Manufacture of electrode for battery |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62105370A (en) * | 1985-10-31 | 1987-05-15 | Shin Kobe Electric Mach Co Ltd | Manufacture of cathode plate for alkaline storage battery |
JPS63105468A (en) * | 1986-10-20 | 1988-05-10 | Sanyo Electric Co Ltd | Manufacture of nickel hydroxide electrode for alkaline storage battery |
JPS63314763A (en) * | 1987-06-17 | 1988-12-22 | Sanyo Electric Co Ltd | Manufacture of nickel hydroxide electrode for alkaline storage battery |
JPH0550100B2 (en) * | 1987-06-17 | 1993-07-28 | Sanyo Electric Co |
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