JPH0318305B2 - - Google Patents
Info
- Publication number
- JPH0318305B2 JPH0318305B2 JP58212211A JP21221183A JPH0318305B2 JP H0318305 B2 JPH0318305 B2 JP H0318305B2 JP 58212211 A JP58212211 A JP 58212211A JP 21221183 A JP21221183 A JP 21221183A JP H0318305 B2 JPH0318305 B2 JP H0318305B2
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- electrode plate
- active material
- cadmium
- negative 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 claims description 69
- 239000000835 fiber Substances 0.000 claims description 32
- 229910052759 nickel Inorganic materials 0.000 claims description 32
- 239000011149 active material Substances 0.000 claims description 19
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 18
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 claims description 18
- 229910052793 cadmium Inorganic materials 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 15
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 238000005520 cutting process Methods 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 8
- 238000003860 storage Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000005245 sintering Methods 0.000 claims description 5
- CXKCTMHTOKXKQT-UHFFFAOYSA-N cadmium oxide Inorganic materials [Cd]=O CXKCTMHTOKXKQT-UHFFFAOYSA-N 0.000 claims description 4
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 4
- 238000011049 filling Methods 0.000 claims description 4
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims description 3
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 2
- 239000003792 electrolyte Substances 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 238000007747 plating Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PLLZRTNVEXYBNA-UHFFFAOYSA-L cadmium hydroxide Chemical compound [OH-].[OH-].[Cd+2] PLLZRTNVEXYBNA-UHFFFAOYSA-L 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- -1 nickel powder Chemical compound 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-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
- H01M4/64—Carriers or collectors
- H01M4/70—Carriers or collectors characterised by shape or form
- H01M4/80—Porous plates, e.g. sintered carriers
-
- 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
-
- 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)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明はアルカリ蓄電池用ペースト式負極板の
製造法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for manufacturing a paste-type negative electrode plate for alkaline storage batteries.
従来技術とその問題点
従来、アルカリ蓄電池用カドミウム負極板とし
ては、ニツケル粉末を穿孔鋼板あるいはニツケル
ネツト等に焼結させた多孔体基板に活物質を充填
させた焼結式極板がよく知られている。この多孔
体基板は、ニツケル粉末を単に穿孔鋼板あるい
は、ニツケルネツト等に焼結させたものであり、
ニツケル粉末粒子間結合が弱く、実用上多孔度80
%程度が限界である。Conventional technology and its problems Conventionally, as a cadmium negative electrode plate for alkaline storage batteries, a sintered type electrode plate in which an active material is filled in a porous substrate made by sintering nickel powder into a perforated steel plate or nickel net has been well known. There is. This porous substrate is simply sintered nickel powder into a perforated steel plate, nickel net, etc.
The bond between nickel powder particles is weak, and the porosity is practically 80.
The limit is about %.
又、これらの多孔体基板は、粒子間結合の弱い
ニツケル粉末を保持するために常に穿孔鋼板、ニ
ツケルネツト等のごとき芯金を必要とし、単位体
積あたりの活物質の充填量が芯金体積分だけ少な
くなる欠点を有している。さらによく知られたる
ごとく、この多孔体は2〜3μの微粉末ニツケル
の焼結体であり、構成される細孔は10μ以下の微
細孔がほとんどである。このため活物質充填方法
は、溶液含浸法に限定され、含浸、中和、水洗、
乾燥の工程を数回繰返し所定量を充填させなけれ
ばならない。このために、極板のコストアツプあ
るいはエネルギー密度の低下に結びついている。 In addition, these porous substrates always require a core metal such as a perforated steel plate or nickel net to hold the nickel powder, which has weak interparticle bonds, and the amount of active material filled per unit volume is equal to the volume of the core metal. It has fewer drawbacks. As is well known, this porous body is a sintered body of finely powdered nickel with a diameter of 2 to 3 microns, and most of the pores are 10 microns or smaller. For this reason, the active material filling method is limited to the solution impregnation method, which includes impregnation, neutralization, water washing,
The drying process must be repeated several times to fill the specified amount. This leads to an increase in the cost of the electrode plate or a decrease in energy density.
この欠点を除去する試みとして、例えば芯金を
もたないニツケルメツキ鉄繊維焼結体、あるいは
電解ニツケルメツキによつて作成された発泡状ニ
ツケル多孔体等に直接固体活物質を充填させる、
いわゆるペースト式充填方法等がなされている。
しかし前者はメツキの不安定性、後者は引張強度
の弱さ等に問題がある。 In an attempt to eliminate this drawback, for example, a solid active material is directly filled into a nickel-plated iron fiber sintered body without a core metal, or a foamed nickel porous body created by electrolytic nickel plating, etc.
A so-called paste filling method has been used.
However, the former has problems such as instability of the plating, and the latter has problems such as low tensile strength.
これらの欠点を改良する金属繊維の製造方法が
提案されている。これはバイト上に線径数mmのニ
ツケル線を移動させながら、さらに細い繊維に切
削するものである。しかしこの製法による場合、
バイトの消耗が激しく、かつ不均一な径の繊維し
か出来ないという欠点があつた。 A method for producing metal fibers has been proposed that improves these drawbacks. This involves moving a nickel wire several millimeters in diameter over a cutting tool while cutting it into even thinner fibers. However, with this manufacturing method,
The drawback was that the cutting tool was severely worn out, and only fibers with uneven diameters could be produced.
又、従来酸化カドミウム、水酸化カドミウム等
の活物質、ニツケル粉末等の電導材および有機溶
剤等をニツケルメツキ穿孔鋼板からなる電導性基
板に塗着乾燥させたペースト式カドミウム電極
は、アルカリ電解液中で化成の充放電処理を施し
ていた。化成により一部に金属カドミウムを残存
させた負極板と放電末のニツケル正極板並びにセ
パレータを共に巻込み、電槽に組み入れ電解液を
注液後封口して、密閉形ニツケルカドミウム電池
として製造されている。もしカドミウムの残存が
なく封口時にすべて水酸化カドミウムである場
合、ニツケル電極に比較し、カドミウム電極の方
が利用率が悪いためカドミウム極側で容量制限を
うける。又、ニツケル極側は充放電サイクルの進
行に伴ない容量劣化がほとんどないのに対し、カ
ドミウム極側は徐々に劣化を示す特性を有するた
め、これを補う意味で余分のカドミウムを残存さ
せるのである。負極容量は初期の劣化が大きい
が、ほぼ60〜80%程度で停止し、それ以後の劣化
は極端に少なくなる。 In addition, conventional paste-type cadmium electrodes, in which active materials such as cadmium oxide and cadmium hydroxide, conductive materials such as nickel powder, and organic solvents are coated and dried on a conductive substrate made of a perforated steel plate with nickel plating, are used in an alkaline electrolyte. It had undergone chemical charging and discharging treatment. The negative electrode plate, in which metal cadmium remains partially due to chemical formation, the discharged nickel positive electrode plate, and the separator are rolled together, placed in a battery case, filled with electrolyte, and sealed, producing a sealed nickel-cadmium battery. There is. If there is no residual cadmium and all cadmium hydroxide is used during sealing, the cadmium electrode has a lower utilization rate than the nickel electrode, so the capacity is limited on the cadmium electrode side. Also, while the nickel electrode side has almost no capacity deterioration as the charge/discharge cycle progresses, the cadmium electrode side has the characteristic of gradually deteriorating, so extra cadmium is left to compensate for this. . The initial deterioration of the negative electrode capacity is large, but it stops after approximately 60 to 80%, and the deterioration thereafter becomes extremely small.
すなわち、活物質の利用率は見かけ上正極がほ
ぼ100%近くであるのに対し、カドミウム極は60
〜80%程度である。 In other words, while the utilization rate of the active material is apparently close to 100% for the positive electrode, it is only 60% for the cadmium electrode.
~80%.
この両者の容量の均衡を保たせるために、上記
化成処理を行なうのである。この工程は複雑なだ
けでなく、従来のペースト式カドミウム極は焼結
式カドミウム極と異なり、化成中に発生するガス
によつて活物質の脱落がしばしば発生する。それ
故にガスの発明しない不完全な部分化成により、
残存カドミウム量をコントロールすることを余儀
無くされた。 In order to maintain a balance between these two capacities, the above-mentioned chemical conversion treatment is performed. This process is not only complicated, but unlike sintered cadmium electrodes in conventional paste-type cadmium electrodes, the active material often falls off due to the gas generated during formation. Therefore, due to uninvented incomplete partial chemical formation of gas,
It was necessary to control the amount of residual cadmium.
発明の目的
本発明は上記従来の問題点に鑑みなされたもの
であり、高性能で低価格かつ生産性の高いアルカ
リ蓄電池用ペースト式負極板を提供することを目
的とするものである。OBJECTS OF THE INVENTION The present invention has been made in view of the above-mentioned conventional problems, and an object thereof is to provide a paste-type negative electrode plate for alkaline storage batteries that is high-performance, low-cost, and highly productive.
発明の構成
本発明は上記目的を達成するべく、
ニツケルのブロツクをびびり振動切削し、ニツ
ケル繊維を製造する工程、
次にニツケル繊維をエアーレード法により均一
分布する工程、
次にニツケル繊維分布体を還元性雰囲気で焼結
し、ニツケル繊維焼結体を得る工程、
次に酸化カドミウム、金属カドミウムにエチレ
ングリコール、カルボキシメチルセルロースを加
えて混合し、スラリー状活物質を調製する工程、
次にニツケル繊維焼結体にスラリー状活物質を
充填する工程、
次に活物質充填極板を部分的に乾燥する工程、
次に部分的に乾燥した極板の厚みを調整する工
程、
次に厚みを調整した極板を乾燥によりエチレン
グリコールを除去する工程、
を有することを特徴とするアルカリ蓄電池用ペー
スト式負極板の製造法である。Structure of the Invention In order to achieve the above-mentioned object, the present invention includes a step of producing nickel fibers by cutting a nickel block by vibration vibration, a step of uniformly distributing the nickel fibers by an air-laid method, and then a step of distributing the nickel fibers into a nickel fiber distribution body. A process of sintering in a reducing atmosphere to obtain a nickel fiber sintered body. Next, a process of adding and mixing ethylene glycol and carboxymethyl cellulose to cadmium oxide and metal cadmium to prepare a slurry active material. Next, a process of sintering the nickel fiber. A step of filling the aggregate with a slurry-like active material, a step of partially drying the active material-filled electrode plate, a step of adjusting the thickness of the partially dried electrode plate, and then a process of adjusting the thickness of the electrode A method for producing a paste-type negative electrode plate for an alkaline storage battery, comprising the step of removing ethylene glycol by drying the plate.
実施例
以下、本発明の詳細について一実施例に基づき
説明する。Example Hereinafter, details of the present invention will be explained based on one example.
ニツケルのブロツクをびびり振動切削して、繊
維径4〜50μmのニツケル繊維を製造する。 Nickel fibers with a fiber diameter of 4 to 50 μm are produced by vibration-cutting a nickel block.
このニツケル繊維を連続的にエアーレード法に
よつて均一に分布し、ニツケル繊維分布体とす
る。 The nickel fibers are continuously and uniformly distributed by an air-laid method to form a nickel fiber distribution body.
このニツケル繊維分布体を還元性雰囲気で、約
1000℃で焼結する。これによつて、ニツケル繊維
焼結体が得られた。第1図a,b(bはaの拡大
図)にニツケル繊維燃焼体の顕微鏡写真を示し
た。びびり振動切削によるニツケル繊維には、第
1図bに示した如く、その繊維表面にびびりマー
クと呼ばれている凸部がある。(第1図bの繊維
面上のしわ状の白い部分)
これによつて、他の製造法の繊維との識別がで
きる。 This nickel fiber distribution body is heated in a reducing atmosphere to approx.
Sinter at 1000℃. As a result, a nickel fiber sintered body was obtained. Figures 1a and 1b (b is an enlarged view of a) show microscopic photographs of the nickel fiber combustion body. The nickel fiber produced by chatter vibration cutting has convex portions called chatter marks on the fiber surface, as shown in FIG. 1b. (Wrinkle-like white area on the fiber surface in FIG. 1b) This allows the fiber to be distinguished from fibers produced by other methods.
尚、繊維焼結体の多孔度は、繊維量、焼結温
度、時間等をコントロールすることによつて85〜
98%程度のものが得られる。 The porosity of the fiber sintered body can be adjusted from 85 to 85 by controlling the amount of fiber, sintering temperature, time, etc.
About 98% can be obtained.
次に酸化カドミウム60〜80wt%、粒子径が0.5
〜1μmの微細粒子からなる金属カドミウム40〜
20wt%をよく混合する。これに5〜9wt%のエチ
レングリコール及び0.6wt%のカルボキシメチル
セルロースを加えてスラリー状活物質を調製す
る。 Next, cadmium oxide 60-80wt%, particle size 0.5
~ Metallic cadmium 40 consisting of fine particles of 1 μm ~
20wt% and mix well. A slurry active material is prepared by adding 5 to 9 wt% ethylene glycol and 0.6 wt% carboxymethyl cellulose.
前記のニツケル繊維焼結体の数十米の連続体を
このスラリー状活物質中に連続的に通過させ、浸
透させることによつて活物質を充填する。 A continuous body of several tens of meters of the above-mentioned nickel fiber sintered body is continuously passed through this slurry-like active material, and is filled with the active material by infiltrating the active material.
その後、極板表面付近が60〜80℃に調整された
赤外線ランプよりなる乾燥機中で部分的に乾燥す
る。ついで、ローラープレスにより所定の厚みに
する。厚み調整後の極板は、温度250℃の熱風乾
燥機を通り、エチレングリコールを完全に除去す
る。最後に極板は希望する電池サイズに見合つた
寸法に切断される。この負極板と、従来の化成処
理によつて完全放置されたシンター式正極板、並
びにポリプロピレン不織布よりなるセパレータ等
を用いて自動的に巻きこまれた後、電槽に挿入さ
れる。その後、水酸化カリウム水溶液に注液し封
口する。封口電池は一昼夜放置することによつ
て、電解液との親和性をもたした後、充放電を行
ない完成電池となる。 Thereafter, the electrode plate surface area is partially dried in a dryer equipped with an infrared lamp adjusted to a temperature of 60 to 80°C. Then, it is made to a predetermined thickness using a roller press. After adjusting the thickness, the electrode plates are passed through a hot air dryer at a temperature of 250°C to completely remove ethylene glycol. Finally, the plates are cut to size appropriate for the desired battery size. This negative electrode plate, a sintered positive electrode plate that has been completely left to undergo conventional chemical conversion treatment, and a separator made of polypropylene nonwoven fabric are automatically rolled up and then inserted into a battery case. After that, a potassium hydroxide aqueous solution is poured into the container and the container is sealed. A sealed battery is left for a day and night to develop compatibility with the electrolyte, and then charged and discharged to become a completed battery.
このように完成されたC型サイズの密閉形ニツ
ケルカドミウム電池と従来の化成処理工程によ
つて作成された焼結式負極板からなる同一サイズ
の密閉形ニツケルカドミウム電池の常温におけ
る寿命を調べたところ、第2図に示すごとく、本
発明による電池の方が容量、並びに寿命共優れて
いることが判明した。 We investigated the lifespan at room temperature of the C-sized sealed nickel-cadmium battery completed in this way and the same-sized sealed nickel-cadmium battery made of a sintered negative electrode plate created by a conventional chemical conversion process. As shown in FIG. 2, it was found that the battery according to the present invention was superior in both capacity and life.
電池容量が向上した原因は、従来の焼結式負極
板のエネルギー密度が、芯金、低多孔度等によつ
て550mAh/c.c.程度であるのに対し、本発明の繊
維式負極板は、704mAh/c.c.と容量密度がかなり
向上したため、余分な容積を正極側にまわすこと
ができ、全体として高容量化電池になる。さらに
微細多孔焼結体を用いた従来形電池の方が寿命が
短かい。この原因は寿命末期電池は負極容量制限
になつており、従来の焼結式電池は微細孔故に、
極板中のカドミウムの凝集に伴ない細孔が閉塞さ
れ、電解液の内部拡散が悪化するためであること
が分つた。本発明の繊維焼結体は芯金もなく、細
孔が大きいため極めて電解液の流通が良好であ
り、負極劣化が少ないことが判明した。 The reason for the improved battery capacity is that while the energy density of conventional sintered negative electrode plates is approximately 550mAh/cc due to the core metal, low porosity, etc., the fiber type negative electrode plate of the present invention has an energy density of 704mAh/cc. Since the capacity density has been significantly improved to /cc, the extra volume can be diverted to the positive electrode side, resulting in a battery with a higher capacity overall. Furthermore, conventional batteries using microporous sintered bodies have a shorter lifespan. The reason for this is that batteries at the end of their lifespan are limited in negative electrode capacity, and conventional sintered batteries have fine pores.
It was found that this was because the pores were blocked due to the agglomeration of cadmium in the electrode plate, worsening internal diffusion of the electrolyte. It was found that the fiber sintered body of the present invention does not have a core metal and has large pores, so that the electrolyte can flow very well, and the negative electrode does not deteriorate much.
本発明のアルカリ蓄電池用ペースト式負極板
は、化成処理工程が不要であり、生産性に優れし
かもペースト式で活物質充填が容易であり低コス
トで生産できる。 The paste-type negative electrode plate for alkaline storage batteries of the present invention does not require a chemical conversion treatment process, has excellent productivity, and is a paste-type negative electrode plate that can be easily filled with active material and can be produced at low cost.
発明の効果
上述した如く、本発明は高性能で低価格かつ生
産性の高いアルカリ蓄電池用ペースト式負極板を
提供できるので、その工業的価値は極めて大であ
る。Effects of the Invention As described above, the present invention can provide a paste-type negative electrode plate for alkaline storage batteries that is high-performance, low-cost, and highly productive, and therefore has extremely great industrial value.
第1図のa,bは本発明のびびり振動切削加工
ニツケル繊維焼結体の顕微鏡写真である。第2図
は本発明電池と従来電池の寿命比較特性曲線図で
ある。
……本発明電池、……従来電池。
FIGS. 1a and 1b are micrographs of a nickel fiber sintered body subjected to chatter vibration cutting according to the present invention. FIG. 2 is a life comparison characteristic curve diagram of the battery of the present invention and a conventional battery. ...battery of the present invention, ...conventional battery.
Claims (1)
ツケル繊維を製造する工程、 次にニツケル繊維をエアーレード法により均一
分布する工程、 次にニツケル繊維分布体を還元性雰囲気で焼結
し、ニツケル繊維焼結体を得る工程、 次に酸化カドミウム、金属カドミウムにエチレ
ングリコール、カルボキシメチルセルロースを加
えて混合し、スラリー状活物質を調製する工程、 次にニツケル繊維焼結体にスラリー状活物質を
充填する工程、 次に活物質充填極板を部分的に乾燥する工程、 次に部分的に乾燥した極板の厚みを調整する工
程、 次に厚み調整した極板を乾燥によりエチレング
リコールを除去する工程、 を有することを特徴とするアルカリ蓄電池用ペー
スト式負極板の製造法。[Claims] 1. A step of producing nickel fibers by vibration-cutting a nickel block, then a step of uniformly distributing the nickel fibers by an air-laid method, and then sintering the nickel fiber distribution body in a reducing atmosphere. Next, a step of adding and mixing ethylene glycol and carboxymethyl cellulose to cadmium oxide and metal cadmium to prepare a slurry-like active material; Next, adding a slurry-like active material to the nickel fiber sintered body. The step of filling the active material-filled electrode plate with a substance, the step of partially drying the electrode plate filled with the active material, the step of adjusting the thickness of the partially dried electrode plate, and the step of drying the thickness-adjusted electrode plate with ethylene glycol. A method for producing a paste-type negative electrode plate for an alkaline storage battery, comprising the step of removing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58212211A JPS60105173A (en) | 1983-11-10 | 1983-11-10 | Paste type negative plate for alkaline storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58212211A JPS60105173A (en) | 1983-11-10 | 1983-11-10 | Paste type negative plate for alkaline storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60105173A JPS60105173A (en) | 1985-06-10 |
| JPH0318305B2 true JPH0318305B2 (en) | 1991-03-12 |
Family
ID=16618766
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58212211A Granted JPS60105173A (en) | 1983-11-10 | 1983-11-10 | Paste type negative plate for alkaline storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60105173A (en) |
-
1983
- 1983-11-10 JP JP58212211A patent/JPS60105173A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60105173A (en) | 1985-06-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4792505A (en) | Electrodes made from mixed silver-silver oxides | |
| JPH0318305B2 (en) | ||
| JPS6329450A (en) | Manufacture of electrode for cell | |
| JP3156485B2 (en) | Nickel electrode for alkaline storage battery | |
| JP4588288B2 (en) | Method for manufacturing substrate for electrode plate, method for manufacturing positive electrode plate, and alkaline storage battery | |
| JP3234492B2 (en) | Non-sintered nickel electrode for alkaline storage batteries | |
| JP3454606B2 (en) | Method for producing positive electrode active material for alkaline storage battery | |
| JPS5819866A (en) | Manufacture of cadmium electrode for secondary battery | |
| JPH0318303B2 (en) | ||
| JP3229800B2 (en) | Non-sintered nickel electrode for alkaline storage batteries | |
| JPH06283162A (en) | Metal hydride electrode, battery and production | |
| JPS60170167A (en) | Manufacturing method for alkaline cell electrode | |
| JP2981537B2 (en) | Negative electrode for alkaline batteries | |
| JPH0429189B2 (en) | ||
| JPH0318304B2 (en) | ||
| JPH0517661B2 (en) | ||
| JP3397216B2 (en) | Nickel plate, method of manufacturing the same, and alkaline storage battery using the same | |
| JP2590437B2 (en) | Electrode substrate for alkaline batteries | |
| JP3384109B2 (en) | Nickel plate | |
| JPH09147908A (en) | Paste type nickel electrode for alkaline storage battery | |
| JPH07335210A (en) | Electrode for alkaline battery | |
| JPS5833665B2 (en) | Manufacturing method of iron electrode | |
| JPH10162835A (en) | Electrode for alkaline storage battery and method for producing the same | |
| JPH10188971A (en) | Unsintered nickel electrode for alkaline storage battery | |
| JPS60216448A (en) | Paste type negative plate for alkaline storage battery |