JPH0619990B2 - Nickel electrode manufacturing method for alkaline batteries - Google Patents
Nickel electrode manufacturing method for alkaline batteriesInfo
- Publication number
- JPH0619990B2 JPH0619990B2 JP59002235A JP223584A JPH0619990B2 JP H0619990 B2 JPH0619990 B2 JP H0619990B2 JP 59002235 A JP59002235 A JP 59002235A JP 223584 A JP223584 A JP 223584A JP H0619990 B2 JPH0619990 B2 JP H0619990B2
- Authority
- JP
- Japan
- Prior art keywords
- cobalt
- acid
- electrode
- nickel
- nickel electrode
- 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 - Lifetime
Links
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims description 28
- 229910052759 nickel Inorganic materials 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 13
- 150000001868 cobalt Chemical class 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 9
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 claims description 7
- 239000000843 powder Substances 0.000 claims description 7
- 239000007864 aqueous solution Substances 0.000 claims description 5
- 239000000243 solution Substances 0.000 claims description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- 229940011182 cobalt acetate Drugs 0.000 claims description 3
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 claims description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- 239000003513 alkali Substances 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims 2
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims 1
- XNZJTLSFOOXUAS-UHFFFAOYSA-N cobalt hydrochloride Chemical compound Cl.[Co] XNZJTLSFOOXUAS-UHFFFAOYSA-N 0.000 claims 1
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims 1
- 229910000152 cobalt phosphate Inorganic materials 0.000 claims 1
- 229940044175 cobalt sulfate Drugs 0.000 claims 1
- 229910000361 cobalt sulfate Inorganic materials 0.000 claims 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 claims 1
- ZBDSFTZNNQNSQM-UHFFFAOYSA-H cobalt(2+);diphosphate Chemical compound [Co+2].[Co+2].[Co+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O ZBDSFTZNNQNSQM-UHFFFAOYSA-H 0.000 claims 1
- 239000011149 active material Substances 0.000 description 23
- 239000002184 metal Substances 0.000 description 11
- 229910052751 metal Inorganic materials 0.000 description 11
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000758 substrate Substances 0.000 description 6
- 229910017052 cobalt Inorganic materials 0.000 description 5
- 239000010941 cobalt Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 230000004913 activation Effects 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- -1 drying Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 235000011118 potassium hydroxide Nutrition 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 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
- 229910001429 cobalt ion Inorganic materials 0.000 description 1
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical compound [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 description 1
- 239000011162 core material Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- UGKDIUIOSMUOAW-UHFFFAOYSA-N iron nickel Chemical compound [Fe].[Ni] UGKDIUIOSMUOAW-UHFFFAOYSA-N 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 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
【発明の詳細な説明】 産業上の利用分野 本発明は、ニッケル−カドミウム、ニッケル−鉄蓄電池
などのアルカリ蓄電池に用いるニッケル電極、特に活物
質の支持体にスポンジ状金属多孔体を用いる電極の改良
に関する。TECHNICAL FIELD The present invention relates to an improvement of a nickel electrode used in an alkaline storage battery such as a nickel-cadmium or nickel-iron storage battery, particularly an electrode using a sponge-like metal porous body as a support of an active material. Regarding
従来例の構成とその問題点 従来、ニッケル−カドミウム蓄電池に代表されるアルカ
リ蓄電池用のニッケル電極は、電極の構造や製法によっ
て、ポケット式,焼結式,ペースト式があり、最近はそ
の他の活物質の支持体として三次元的に連続した構造を
もつ金属のスポンジ状多孔体を用いた発泡メタル式が提
案されている。Conventional configuration and its problems Conventionally, nickel electrodes for alkaline storage batteries, typified by nickel-cadmium storage batteries, have a pocket type, a sintering type, and a paste type, depending on the structure and manufacturing method of the electrode. A foam metal type using a metal sponge-like porous body having a three-dimensionally continuous structure as a support for a substance has been proposed.
これらのうち、発泡メタル式は支持体となるスポンジ状
金属多孔体の構造が焼結式の基板と同様に三次元の網目
状であることから、焼結式電極の場合と同じく電子伝導
がすぐれているので、焼結式電極に匹敵する放電性能や
寿命特性が得られる。しかも、スポンジ状金属多孔体の
場合、孔径は数十μから数mmの範囲において任意のもの
が選択できるので、孔径が数百μの多孔体を基板として
選定し、活物質に粒径が数μから百数十μに分布した粉
末を用いれば直接充填することができる。したがって、
ペースト式電極の塗着に近い方法が採用でき、製法的に
簡単である。さらに、基板の空孔率は95%前後と高く
焼結式よりも活物質の高密度充填が可能である。なお、
焼結式基板は空孔率が80%前後で、孔数が数μか数十
μであるので活物質の直接充填は困難で、塩溶液による
充填が一般的である。Among them, the foam metal type has a three-dimensional mesh-like structure of the sponge-like metal porous body as the support, which is similar to that of the sintered type substrate, and therefore has the same excellent electron conduction as that of the sintered type electrode. Therefore, the discharge performance and life characteristics comparable to those of the sintered electrode can be obtained. Moreover, in the case of a sponge-like metal porous body, any pore size can be selected within the range of several tens of μ to several mm, so a porous body with a pore size of several hundred μ is selected as the substrate, and the active material has a particle size of several μm. The powder can be directly filled by using the powder distributed from μ to hundreds of tens μ. Therefore,
A method similar to the pasting of paste type electrodes can be adopted, and the manufacturing method is simple. Furthermore, the porosity of the substrate is as high as around 95%, and the active material can be packed at a higher density than in the sintering method. In addition,
Since the sintered substrate has a porosity of about 80% and the number of holes is several μm or several tens μm, direct filling of the active material is difficult, and filling with a salt solution is common.
発泡メタル式電極は一般的に次に示す工程を経て製作さ
れていた。 基板に電極リード取付部を加圧による形
成、 水酸化ニッケル粉末を主とする活物質をペース
ト状混合物にして基板多孔部内部への充填、 加圧に
よる活物質の充填密度の向上と保持、 乾燥、 結
着剤の添加による充填物保持の補強、 乾燥、 リ
ード板取付 このようにして得られるニッケル電極は活物質である水
酸化ニッケルを直接充填しているので、焼結式の場合に
必要な転化処理および化成処理を施さずに電池に組み込
み用いることができる。The foam metal type electrode is generally manufactured through the following steps. The electrode lead attachment part is formed on the substrate by pressing, the active material mainly of nickel hydroxide powder is made into a paste-like mixture and is filled inside the porous part of the substrate, the packing density of the active material is improved and kept by pressing, and dried. Reinforcement of retention of filler by addition of binder, drying, lead plate mounting The nickel electrode thus obtained is directly filled with nickel hydroxide, which is the active material. It can be incorporated into a battery without being subjected to conversion treatment and conversion treatment.
しかし、その反面活物質の水酸化ニッケルが電気化学的
な活性化を充分にされた状態ではない。However, on the other hand, nickel hydroxide, which is an active material, is not in a state where the electrochemical activation is sufficiently performed.
電池で充放電を充分にくり返すことによって、活性化が
進行すると活物質の利用率は90%をこえるが、初期の
充放電においては活物質の利用率が75%から90%の
範囲にあって、バラツキの幅が大きい。また、充放電を
繰り返しても利用率が向上しない場合もあった。The utilization rate of the active material exceeds 90% as the activation progresses by sufficiently repeating the charge and discharge in the battery, but the utilization rate of the active material is in the range of 75% to 90% in the initial charge and discharge. And there is a wide range of variation. In addition, the utilization rate may not be improved even after repeated charging and discharging.
なお、このようなペースト式電極の利用率を大きくする
ためにコバルトイオンが有効であることが知られてお
り、しかも、コバルトを塩の形で添加するとコバルト粉
末の場合よりも少ない量で同様の効果が得られる。しか
し、その場合コバルト塩のアニオンイオン除去のための
水洗を十分に行う必要があり、水を多量に消費するとい
う問題点があった。It is known that cobalt ions are effective for increasing the utilization rate of such a paste-type electrode, and when cobalt is added in the form of salt, a similar amount can be obtained with a smaller amount than in the case of cobalt powder. The effect is obtained. However, in this case, it was necessary to sufficiently wash the cobalt salt with water to remove anions, and there was a problem that a large amount of water was consumed.
発明の目的 本発明は、スポンジ状金属多孔体内部に水酸化ニッケル
を主とする活物質粉末を直接充填して得るニッケル電極
の活物質の利用率向上と安定化を簡単な方法で提供する
ことを目的とする。An object of the present invention is to provide a simple method for improving the utilization rate and stabilizing of the active material of the nickel electrode obtained by directly filling the active material powder mainly containing nickel hydroxide into the sponge-like metal porous body. With the goal.
発明の構成 本発明は、少なくとも水酸化ニッケル粉末とニッケル粉
末およびコバルト粉末を含む混合物をスポンジ状金属多
孔体内部に充填後、酸およびコバルト塩の単独あるい
は、両者を少量含む溶液を含浸し、含水状態で高温雰囲
気に放置し、ついでアルカリ溶液中に浸漬してコバルト
塩を水酸化物に転化することを特徴とするものである。Composition of the Invention The present invention is to fill a mixture containing at least nickel hydroxide powder and nickel powder and cobalt powder into a sponge-like metal porous body, and then impregnate a solution containing an acid and a cobalt salt alone or with a small amount of both, to obtain a water content. In this state, it is left in a high temperature atmosphere and then immersed in an alkaline solution to convert the cobalt salt into a hydroxide.
すなわち、この操作によりペースト中に酸を添加して、
ペーストに用いられたコバルトを酸によって一部をコバ
ルト塩にかえ、アルカリ中で水酸化物に転化することに
よって、コバルトを塩で添加した場合と同様の効果を得
ることができる。That is, by adding acid to the paste by this operation,
By partially converting the cobalt used in the paste with an acid into a cobalt salt and converting it into a hydroxide in an alkali, the same effect as when cobalt is added as a salt can be obtained.
この場合、添加する酸あるいはコバルト塩を少量にする
ことによって、転化後のアニオンイオンの除去を容易に
する。その反面転化後、直ちに転化した場合は、添加効
果が十分に発揮されない。そこで、添加後含水状態で少
なくとも12時間放置することで、この問題は十分に解
決できることを見い出した。In this case, the addition of a small amount of acid or cobalt salt facilitates the removal of anion ions after conversion. On the other hand, if it is converted immediately after the conversion, the effect of addition is not sufficiently exhibited. Therefore, it was found that this problem can be sufficiently solved by leaving it in a water-containing state for at least 12 hours after the addition.
この放置においての温度は高い温度が望ましく、実用上
50〜100℃の範囲が適切であり、この範囲で任意に
設定すればよい。It is desirable that the temperature during the standing is high, and a range of 50 to 100 ° C. is suitable for practical use, and the temperature may be arbitrarily set within this range.
以下、本発明の実施例を説明する。Examples of the present invention will be described below.
実施例の説明 活物質の支持体には、材質がニッケルからなる第1図に
示す構造の厚みが1.3mm、多孔度95%、孔径100
〜500μのスポンジ状の多孔体を用いた。同図におい
て、1は芯材部のニッケル、2は空孔部を示す。Description of Examples For the support of the active material, the structure shown in FIG. 1 made of nickel had a thickness of 1.3 mm, a porosity of 95%, and a pore diameter of 100.
A sponge-like porous body of ˜500 μm was used. In the figure, 1 is nickel of the core material, and 2 is a hole.
上記多孔体に水酸化ニッケル粉末81重量%、ニッケル
粉末15重量%、コバルト粉末4重量%の混合物を含水
量約35重量%のペースト状にして均一に充填し、多孔
体表面に付着した余剰ペーストを除去して活物質充填多
孔体として寸法80×240mmを得た。これを加圧後、
酢酸コバルト0.1モル/の水溶液を含浸した電極A
と、Aに用いたのと同濃度の水溶液にさらに酢酸0.1
モル/を加えた溶液に含浸した電極B、および酢酸0.
1モル/の水溶液に含浸した電極Cを作成した。これら
A,B,Cを含水状態で水分の蒸発を防止しながら2
0,50,80、100℃の雰囲気に12時間放置した。
ついで乾燥後、比重1.05のか性カリ水溶液中に10
分間浸漬し、水洗、乾燥を行った。次いで結着剤として
4フッ化エチレンの懸濁液を添加し、寸法40×60mm
に切断加工を行った。Excess paste adhered to the surface of the porous body by uniformly filling the above porous body with a mixture of 81% by weight of nickel hydroxide powder, 15% by weight of nickel powder and 4% by weight of cobalt powder in the form of a paste having a water content of about 35% by weight. Were removed to obtain a size 80 × 240 mm as an active material-filled porous body. After pressurizing this,
Electrode A impregnated with 0.1 mol / cobalt acetate aqueous solution
And 0.1% acetic acid in an aqueous solution of the same concentration used for A.
Electrode B impregnated in a solution containing mol / mol, and acetic acid 0.
An electrode C impregnated with a 1 mol / aqueous solution was prepared. These A, B, C are contained in a water-containing state while preventing evaporation of water.
It was left for 12 hours in an atmosphere of 0, 50, 80 and 100 ° C.
Then, after drying, 10 in a caustic potash solution with a specific gravity of 1.05
It was immersed for a minute, washed with water and dried. Then add a suspension of tetrafluoroethylene as a binder and measure 40 × 60 mm
Was cut into pieces.
つぎに、これらの電極板A,B,Cと無処理の電極Dを
正極とし、負極に公知のカドミウム極、セパレータにポ
リアミド不織布、電解液に水酸化リチウムを含む30%
濃度のか性カリ水溶液を用いて、単3形の電池を構成し
た。Next, these electrode plates A, B and C and the untreated electrode D were used as positive electrodes, the negative electrode was a known cadmium electrode, the separator was polyamide nonwoven fabric, and the electrolyte solution was 30% containing lithium hydroxide.
AA batteries were constructed using a concentrated caustic potash solution.
電池は周囲温度20℃で充電を1/10Cの電流で160
%、放電を電流1/5Cで、1.0Vまでの条件として充
放電試験をくり返した。それぞれの電池について、放電
容量から、正極の理論容量(Ni(OH)21g当り289m
hとして算出)に対する活物質利用率を求めて性能を評
価した。Battery can be charged at an ambient temperature of 20 ° C with a current of 1 / 10C 160
%, The discharge was repeated at a current of 1/5 C up to 1.0 V. From the discharge capacity of each battery, the theoretical capacity of the positive electrode (289 m per 1 g of Ni (OH) 2
The performance was evaluated by obtaining the active material utilization rate (calculated as h).
第2図は本発明における電極Bの放置温度と活物質利用
率との関係を示した図である。FIG. 2 is a diagram showing the relationship between the standing temperature of the electrode B and the active material utilization rate in the present invention.
同図において、活物質利用率は十分に安定した10サイク
ル目を示す。同図からも明らかなように高温の雰囲気に
放置することで放電特性が向上する。これは、50〜8
0℃の高温の条件ではペースト中のコバルトの溶解が促
進された結果であり、室温附近の温度では同様の効果を
得るには2日以上を要する。また、100℃の雰囲気で
は電極板中の水分蒸発が多くなるので、逆に放電特性が
若干低下する傾向にある。In the same figure, the active material utilization rate shows the sufficiently stable 10th cycle. As is clear from the figure, the discharge characteristics are improved by leaving it in a high temperature atmosphere. This is 50-8
This is because the dissolution of cobalt in the paste was promoted under the high temperature condition of 0 ° C., and it took two days or more to obtain the same effect at a temperature near room temperature. Further, in the atmosphere of 100 ° C., the water content in the electrode plate is more likely to be evaporated, so that the discharge characteristics tend to be slightly deteriorated.
第3図は、本発明の電極板A,B,Cを雰囲気80℃で
12時間放置した条件の電池と、従来処方の電極板Dの
充放電サイクルと活物質利用率との関係を示した図であ
る。A,B,Cの本発明の電極を用いた電池は、いずれ
も95%前後の性能を示し、100サイクルの時点にお
いても放電性能の低下はほとんど認められない。一方、
従来処方の電極Dを用いた電池は利用率が85%前後と
充放電のくり返しで放電特性の向上は認められず、低い
性能で安定化する。含浸するコバルト塩や酸の水溶液の
濃度が高すぎる場合、電極中のアニオンの残留により自
己放電特性の劣化などの不具合いを生じるため、濃度は
0.2モル/以下が適切である。電極性能に及ぼす含
浸後の放置時間は放置温度により変化するが、12時間
以上であれば高い活物質利用率が安定して得られる。FIG. 3 shows the relationship between the charge / discharge cycle and the active material utilization rate of a battery under the conditions in which the electrode plates A, B and C of the present invention were left to stand at 80 ° C. for 12 hours, and the electrode plate D of the conventional formulation. It is a figure. The batteries using the electrodes of A, B, and C of the present invention all showed a performance of about 95%, and almost no deterioration in discharge performance was observed even after 100 cycles. on the other hand,
The battery using the electrode D of the conventional formulation has a utilization rate of around 85%, and no improvement in discharge characteristics is observed due to repeated charging / discharging, and is stabilized with low performance. If the concentration of the aqueous solution of the cobalt salt or acid to be impregnated is too high, residual anions in the electrode may cause problems such as deterioration of self-discharge characteristics. Therefore, the concentration is preferably 0.2 mol / or less. The standing time after impregnation, which affects the electrode performance, varies depending on the standing temperature, but if it is 12 hours or more, a high active material utilization rate can be stably obtained.
また、前記実施例ではコバルト塩および酸は酢酸コバル
トおよび酢酸を用いたが、他に一般の酸である硝酸,塩
酸,リン酸,ギ酸などのコバルトを溶解する酸および、
それらのコバルト塩を用いても同様の効果が得られる。Further, although cobalt acetate and acetic acid were used as the cobalt salt and the acid in the above-mentioned examples, other common acids such as nitric acid, hydrochloric acid, phosphoric acid, and formic acid, which dissolve cobalt, and
Similar effects can be obtained by using those cobalt salts.
発明の効果 以上述べたように本発明の方法はこれまで簡単ではある
が活物質利用率で問題があった、スポンジ状金属多孔体
に活物質をペースト状で充填するニッケル電極の性能
を、簡単な方法で容易に向上させることができるもので
ある。EFFECTS OF THE INVENTION As described above, the method of the present invention is simple but has a problem in the active material utilization rate. The performance of the nickel electrode for filling the sponge-like metal porous body with the active material in the form of a paste is simple. It can be easily improved by various methods.
第1図は本発明の実施例に用いたスポンジ状金属多孔体
の拡大図、第2図は本発明の電極の放置雰囲気温度と活
物質利用率との関係を示した図、第3図は本発明の電極
と従来処方の電極を用いた電池の充放電に伴う活物質利
用率の変化を示した図である。FIG. 1 is an enlarged view of a sponge-like metal porous body used in an example of the present invention, FIG. 2 is a view showing a relationship between an ambient temperature of an electrode of the present invention and an active material utilization rate, and FIG. FIG. 4 is a diagram showing changes in active material utilization rate with charge and discharge of a battery using the electrode of the present invention and an electrode of a conventional formulation.
フロントページの続き (72)発明者 増井 基秀 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 山賀 実 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 海谷 英男 大阪府門真市大字門真1006番地 松下電器 産業株式会社内Front page continuation (72) Inventor Motohide Masui 1006 Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Minoru Yamaga 1006 Kadoma, Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd. (72) Inventor Hideo Kaitani 1006 Kadoma, Kadoma-shi, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.
Claims (4)
粉末,ニッケル粉末,コバルト粉末を含むペースト状混
合物を塗着した後、コバルト塩あるいは酸およびこれら
の混合物を含む溶液を含浸し、その後含水状態で50〜
100℃の雰囲気に少なくとも12時間放置し、次いで
アルカリ中に浸漬することを特徴とするアルカリ電池用
ニッケル電極の製造法。1. A conductive porous material is coated with a paste-like mixture containing at least nickel hydroxide powder, nickel powder and cobalt powder, and then impregnated with a solution containing a cobalt salt or an acid and a mixture thereof, and then a water-containing state. And 50 ~
A method for producing a nickel electrode for an alkaline battery, which comprises leaving it in an atmosphere of 100 ° C. for at least 12 hours and then immersing it in an alkali.
ト,リン酸コバルト,塩酸コバルト,硫酸コバルトより
なる群から選択されたいずれかである特許請求の範囲第
1項記載のアルカリ電池用ニッケル電極の製造法。2. The production of a nickel electrode for an alkaline battery according to claim 1, wherein the cobalt salt is any one selected from the group consisting of cobalt acetate, cobalt nitrate, cobalt phosphate, cobalt hydrochloride and cobalt sulfate. Law.
なる群から選択されたいずれかである特許請求の範囲第
1項記載のアルカリ電池用ニッケル電極の製造法。3. The method for producing a nickel electrode for an alkaline battery according to claim 1, wherein the acid is selected from the group consisting of acetic acid, nitric acid, phosphoric acid, hydrochloric acid and sulfuric acid.
2モル/以下である特許請求の範囲第1項から第3項
のいずれかに記載のアルカリ電池用ニッケル電極の製造
法。4. The concentration of the aqueous solution of cobalt salt and acid is 0.
The method for producing a nickel electrode for an alkaline battery according to any one of claims 1 to 3, wherein the amount is 2 mol / or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59002235A JPH0619990B2 (en) | 1984-01-10 | 1984-01-10 | Nickel electrode manufacturing method for alkaline batteries |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59002235A JPH0619990B2 (en) | 1984-01-10 | 1984-01-10 | Nickel electrode manufacturing method for alkaline batteries |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60146453A JPS60146453A (en) | 1985-08-02 |
| JPH0619990B2 true JPH0619990B2 (en) | 1994-03-16 |
Family
ID=11523687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59002235A Expired - Lifetime JPH0619990B2 (en) | 1984-01-10 | 1984-01-10 | Nickel electrode manufacturing method for alkaline batteries |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0619990B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2670609B1 (en) * | 1990-12-13 | 1995-07-07 | Sorapec | NICKEL POSITIVE ELECTRODE. |
| JPH04126339U (en) * | 1991-05-01 | 1992-11-18 | 船井電機株式会社 | video tape recorder |
-
1984
- 1984-01-10 JP JP59002235A patent/JPH0619990B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60146453A (en) | 1985-08-02 |
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