JPH0422065A - Manufacture of cadmium negative electrode for alkaline storage battery - Google Patents
Manufacture of cadmium negative electrode for alkaline storage batteryInfo
- Publication number
- JPH0422065A JPH0422065A JP2125373A JP12537390A JPH0422065A JP H0422065 A JPH0422065 A JP H0422065A JP 2125373 A JP2125373 A JP 2125373A JP 12537390 A JP12537390 A JP 12537390A JP H0422065 A JPH0422065 A JP H0422065A
- Authority
- JP
- Japan
- Prior art keywords
- cadmium
- paste
- metal
- negative electrode
- active material
- 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.)
- Granted
Links
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 title claims abstract description 84
- 229910052793 cadmium Inorganic materials 0.000 title claims abstract description 74
- 238000003860 storage Methods 0.000 title claims description 15
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 238000000034 method Methods 0.000 claims abstract description 32
- 239000011149 active material Substances 0.000 claims abstract description 23
- 238000002156 mixing Methods 0.000 claims abstract description 16
- CXKCTMHTOKXKQT-UHFFFAOYSA-N cadmium oxide Inorganic materials [Cd]=O CXKCTMHTOKXKQT-UHFFFAOYSA-N 0.000 claims abstract description 15
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000001035 drying Methods 0.000 claims abstract description 13
- 239000000758 substrate Substances 0.000 claims description 8
- 239000002184 metal Substances 0.000 abstract description 49
- 229910052751 metal Inorganic materials 0.000 abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 229910044991 metal oxide Inorganic materials 0.000 abstract 2
- 150000004706 metal oxides Chemical class 0.000 abstract 2
- 239000007772 electrode material Substances 0.000 abstract 1
- 230000002401 inhibitory effect Effects 0.000 abstract 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 23
- 230000000052 comparative effect Effects 0.000 description 11
- 229910052759 nickel Inorganic materials 0.000 description 9
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000001768 carboxy methyl cellulose Substances 0.000 description 4
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 4
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 229910001882 dioxygen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 3
- 238000007747 plating Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229920002972 Acrylic fiber Polymers 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 150000001661 cadmium Chemical class 0.000 description 2
- WLZRMCYVCSSEQC-UHFFFAOYSA-N cadmium(2+) Chemical compound [Cd+2] WLZRMCYVCSSEQC-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920005596 polymer binder Polymers 0.000 description 2
- 239000002491 polymer binding agent Substances 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 description 1
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical group [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- LHQLJMJLROMYRN-UHFFFAOYSA-L cadmium acetate Chemical compound [Cd+2].CC([O-])=O.CC([O-])=O LHQLJMJLROMYRN-UHFFFAOYSA-L 0.000 description 1
- PLLZRTNVEXYBNA-UHFFFAOYSA-L cadmium hydroxide Chemical compound [OH-].[OH-].[Cd+2] PLLZRTNVEXYBNA-UHFFFAOYSA-L 0.000 description 1
- -1 cadmium metals Chemical class 0.000 description 1
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 1
- QCUOBSQYDGUHHT-UHFFFAOYSA-L cadmium sulfate Chemical compound [Cd+2].[O-]S([O-])(=O)=O QCUOBSQYDGUHHT-UHFFFAOYSA-L 0.000 description 1
- 229910000331 cadmium sulfate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 1
- 229910001453 nickel ion Inorganic materials 0.000 description 1
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- 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
- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
[発明の目的]
(産業上の利用分野)
本発明は、アルカリ蓄電池用カドミウム負極の製造法に
関する。DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Field of Application) The present invention relates to a method for manufacturing a cadmium negative electrode for an alkaline storage battery.
(従来の技術)
近年、アルカリ蓄電池においてカドミウム負極か用いら
れている。特にペースト式カドミウム負極は、焼結式の
ものと比べて製造工程か簡単で低コストで生産でき、し
かも高エネルギー密度を得ることができるなどの長所を
有するため、多用されている。(Prior Art) In recent years, cadmium negative electrodes have been used in alkaline storage batteries. In particular, paste-type cadmium negative electrodes are widely used because they have advantages such as a simpler manufacturing process, lower cost, and higher energy density than sintered-type ones.
従来、ペースト式カドミウム負極を有するアルカリ蓄電
池は、正極の容量よりもカドミウム負極の放電状態の容
量を大きくすることにより、充電時には正極が先に満充
電となりこの正極から発生する酸素ガスをカドミウム負
極で消費し、かつカドミウム負極は満充電に至らす水素
ガスが発生しないように設計されている。例えば、密閉
型ニッケルカドミウム蓄電池では一般にニッケル正極の
容量に対してカドミウム負極の放電状態の容量を2倍程
度にしている。一方、放電時にはカドミウム負極規制に
なると高率放電特性やサイクル特性か著しく悪化するた
め、カドミウム負極の一部を充電状態にする化成を行な
うことにより、活物質であるカドミウム酸化物の一部を
充電状態(放電予備)の金属カドミウムに変換し、正極
規制になるように設計されている。Conventionally, alkaline storage batteries with paste-type cadmium negative electrodes have a discharged capacity of the cadmium negative electrode larger than the capacity of the positive electrode, so that the positive electrode is fully charged first during charging, and the oxygen gas generated from the positive electrode is absorbed by the cadmium negative electrode. The cadmium negative electrode is designed to prevent the generation of hydrogen gas that would lead to full charge. For example, in a sealed nickel-cadmium storage battery, the discharged capacity of the cadmium negative electrode is generally about twice the capacity of the nickel positive electrode. On the other hand, during discharge, if the cadmium negative electrode is regulated, the high rate discharge characteristics and cycle characteristics will be significantly deteriorated, so by performing chemical formation that places part of the cadmium negative electrode in a charged state, a part of the cadmium oxide, which is the active material, is charged. It is designed to convert into metallic cadmium in the state (discharge reserve) and become a positive electrode regulation.
しかしながら、前述した化成工程は、大きな使用電力及
び繁雑な工程を要し、更に洗浄廃液の処理問題が発生し
、しかも充電状態である金属カドミウムを均一に分布さ
せることが困難であるという問題がある。However, the above-mentioned chemical conversion process requires a large amount of power and is a complicated process, and there are also problems in processing cleaning waste liquid, and furthermore, it is difficult to uniformly distribute metallic cadmium in a charged state. .
かかる問題を解決するため、カドミウム負極内に予め放
電予備としての金属カドミウムを添加し、前記化成工程
を省略した製造方法が提案されて(為る。In order to solve this problem, a manufacturing method has been proposed in which metallic cadmium is added in advance as a discharge reserve into the cadmium negative electrode, and the chemical formation step is omitted.
しかしながら、前記方法で製造されたカドミウム負極は
、以下の理由により電極の利用率を十分に向上てきない
という問題があった。即ち、前記方法は活物質のカドミ
ウム酸化物と共に金属カドミウムを配合してペーストを
調製し、このペーストをパンチトメタルなどの導電性基
板に塗布、乾燥することによってカドミウム負極を得る
方法である。ここで使用される金属カドミウムとしては
、湿式法或いは乾式法により得られた金属カドミウム粉
末があり、湿式法による金属カドミウム粉末は水洗、乾
燥して使用される。前記の湿式法による金属カドミウム
粉末は、一般に海綿状で表面積か大きいため、乾式法に
よる金属カドミウム粉末が球状で表面積が小さいのと比
べると、放電予備としての活性度が高いという利点を有
する。ところが、いずれの金属カドミウム粉末もその表
面かペースト調製前に空気中の酸素や水分と反応し、該
表面に電気化学的に安定な酸化物或いは水酸化物の被膜
が形成される。このため、得られるカドミウム負極は、
金属カドミウムを放電予備として配合したにもかかわら
ず本来の放電予備としての活性が損なわれて導電パスが
なくなり、活物質問の導電性か低下して利用率が低下す
るという問題があった。However, the cadmium negative electrode manufactured by the above method has a problem in that the utilization rate of the electrode cannot be sufficiently improved for the following reasons. That is, the method is a method in which a paste is prepared by blending metal cadmium with cadmium oxide as an active material, and a cadmium negative electrode is obtained by applying this paste to a conductive substrate such as punched metal and drying it. The metal cadmium used here includes metal cadmium powder obtained by a wet method or a dry method, and the metal cadmium powder obtained by the wet method is used after washing with water and drying. The metal cadmium powder produced by the wet process is generally spongy and has a large surface area, so compared to the spherical metal cadmium powder produced by the dry process which has a small surface area, it has the advantage of being highly active as a discharge reserve. However, the surface of any metal cadmium powder reacts with oxygen or moisture in the air before the paste is prepared, and an electrochemically stable oxide or hydroxide film is formed on the surface. Therefore, the obtained cadmium negative electrode is
Despite the inclusion of metallic cadmium as a discharge reserve, there was a problem in that the original activity as a discharge reserve was lost, there was no conductive path, and the conductivity of the active material was reduced, resulting in a lower utilization rate.
一方、カドミウム負極の表面にメツキ処理などを施して
ニッケルや炭素などの導電層を形成し、電極表面の導電
性を向上させて利用率を高める方法も提案されているが
、製造工程が複雑になってコスト面で不利となるという
問題があった。On the other hand, a method has also been proposed in which the surface of the cadmium negative electrode is plated to form a conductive layer of nickel, carbon, etc. to improve the conductivity of the electrode surface and increase the utilization rate, but this method complicates the manufacturing process. Therefore, there was a problem in that it was disadvantageous in terms of cost.
(発明が解決しようとする課題)
本発明は、従来の問題点を解決するためになされたもの
で、利用率を向上したアルカリ蓄電池用カドミウム負極
を容易に製造し得る方法を提供しようとするものである
。(Problems to be Solved by the Invention) The present invention has been made in order to solve the conventional problems, and aims to provide a method for easily manufacturing a cadmium negative electrode for alkaline storage batteries with improved utilization rate. It is.
[発明の構成コ
(課題を解決するための手段)
本発明は、カドミウム酸化物を活物質として配合し、か
つ湿式法により得られた金属カドミウムを湿潤状態で配
合してペーストを調製する工程と、導電性基板上に前記
ペーストを塗布、乾燥する工程とを具備することを特徴
とするアルカリ蓄電池用カドミウム負極の製造法である
。[Structure of the Invention (Means for Solving the Problems) The present invention comprises a step of preparing a paste by blending cadmium oxide as an active material and blending metallic cadmium obtained by a wet method in a wet state. A method for producing a cadmium negative electrode for an alkaline storage battery, comprising the steps of applying the paste on a conductive substrate and drying it.
また、本発明に係る別の発明は、カドミウム酸化物を活
物質として配合して第1のペーストを調製する工程と、
導電性基板上に前記ペーストを塗布、乾燥して活物質層
を形成する工程と、湿式法により得られた金属カドミウ
ムを湿潤状態で配合して第2のペーストを調製する工程
と、前記活物質層上に前記第2のペーストを塗布、乾燥
する工程とを具備することを特徴とするアルカリ蓄電池
用カドミウム負極の製造法である。Another invention according to the present invention includes a step of preparing a first paste by blending cadmium oxide as an active material;
a step of applying and drying the paste on a conductive substrate to form an active material layer; a step of preparing a second paste by blending metal cadmium obtained by a wet method in a wet state; This is a method for producing a cadmium negative electrode for an alkaline storage battery, comprising the steps of applying the second paste on the layer and drying it.
前記カドミウム酸化物としては、例えば酸化カドミウム
、水酸化カドミウムなどが挙げられる。Examples of the cadmium oxide include cadmium oxide and cadmium hydroxide.
前記湿式法は、カドミウムイオンを含む溶液中での置換
反応により金属カドミウムを得る方法である。かかる湿
式法としては、例えば硫酸カドミウムや酢酸カドミウム
等のカドミウム塩溶液に、亜鉛及びニッケル粉末やニッ
ケルイオンを添加し、該カドミウム塩溶液中のカドミウ
ムイオンを亜鉛イオンで置換することにより、金属ニッ
ケルを含有する金属カドミウムを得る方法が挙げられる
。The wet method is a method for obtaining metal cadmium by a substitution reaction in a solution containing cadmium ions. In such a wet method, for example, zinc and nickel powder or nickel ions are added to a cadmium salt solution such as cadmium sulfate or cadmium acetate, and the cadmium ions in the cadmium salt solution are replaced with zinc ions to remove metallic nickel. A method for obtaining the metal cadmium contained therein is mentioned.
前記金属カドミウムの湿潤状態としては、含水率(金属
カドミウム量に対する水分量)を5重量%以上にするこ
とが望ましい。この理由は、含水率を5重量%未満にす
ると金属カドミウム表面が酸化されて活性度が低下して
電極の利用率が低下する恐れがある。また、発火を防止
する観点からも含水率の下限値を5重量%にすることが
適している。なお、含水率の上限値は目的とする粘性の
ペーストが得られるようにペーストの成分に応じて適宜
に設定すればよい。As for the wet state of the metal cadmium, it is desirable that the moisture content (the amount of water relative to the amount of metal cadmium) be 5% by weight or more. The reason for this is that if the water content is less than 5% by weight, the surface of the metal cadmium will be oxidized, the activity will decrease, and there is a risk that the utilization rate of the electrode will decrease. Further, from the viewpoint of preventing ignition, it is suitable to set the lower limit of the water content to 5% by weight. Note that the upper limit of the water content may be appropriately set according to the components of the paste so that a paste with the desired viscosity can be obtained.
前記導電性基板としては、例えばパンチトメタル、エキ
スバンドメタル、金網等の二次元構造のもの、発泡メタ
ル、網状焼結金属繊維などの三次元構造のものなどを挙
げることができる。Examples of the conductive substrate include those with a two-dimensional structure such as punched metal, expanded metal, and wire mesh, and those with a three-dimensional structure such as foamed metal and reticulated sintered metal fiber.
前記ペーストは、前記カドミウム酸化物や金属カドミウ
ムのほかに、通常、高分子結着剤、導電材などを水や有
機溶媒下で配合して調製される。The paste is usually prepared by blending a polymer binder, a conductive material, etc. in water or an organic solvent in addition to the cadmium oxide and metal cadmium.
前記高分子結着剤としては、例えばカルボキシメチルセ
ルロース、アクリル短繊維、ポリビニルアルコール、ポ
リアクリル酸ソーダなどが挙げられる。Examples of the polymer binder include carboxymethyl cellulose, short acrylic fibers, polyvinyl alcohol, and sodium polyacrylate.
前記導電材としては、例えばカーボニルニッケル、カー
ボンブラック、黒鉛等の導電材などが挙げられる。Examples of the conductive material include conductive materials such as carbonyl nickel, carbon black, and graphite.
(作用)
本発明によれば、カドミウム酸化物を活物質として配合
し、かつ湿式法により得られた金属カドミウムを湿潤状
態で配合してペーストを調製することによって、前記ペ
ースト中の金属カドミウムの表面が空気に直接的に接触
するのを回避できるため、金属カドミウムの表面に酸化
物或いは水酸化物の被膜が形成されるのを防止できる。(Function) According to the present invention, by preparing a paste by blending cadmium oxide as an active material and blending metallic cadmium obtained by a wet method in a wet state, the surface of metallic cadmium in the paste is Since direct contact with air can be avoided, formation of an oxide or hydroxide film on the surface of metal cadmium can be prevented.
このため、前記ペーストを導電性基板上に塗布、乾燥す
ることにより、前記活物質と共に金属カドミウムを高活
性のまま維持できる。その結果、活物質問の導電性を阻
害せずに放電予備として良好に機能する金属カドミウム
を含み、利用率が向上されたアルカリ蓄電池用カドミウ
ム負極を容易に製造することかできる。Therefore, by applying the paste onto a conductive substrate and drying it, metal cadmium can be maintained at a high level of activity together with the active material. As a result, it is possible to easily produce a cadmium negative electrode for an alkaline storage battery that contains metal cadmium that functions well as a discharge reserve without impeding the conductivity of the living material and has an improved utilization rate.
一方、本発明に係る別の発明によれば、湿式法により得
られた金属カドミウムを湿潤状態のままで配合してペー
ストを調製することによって、前記ペースト中の金属カ
ドミウムの表面が空気に直接的に接触するのを回避でき
るため、金属カドミウムの表面に酸化物或いは水酸化物
の被膜が形成されるのを防止できる。このため、導電性
基板上に形成され、かつカドミウム酸化物を活物質とし
て含む活物質層上に、前記ペーストを塗布、乾燥するこ
とにより、前記活物質と共に金属カドミウムを高活性の
まま維持できる。その結果、活物質問の導電性を阻害せ
ずに放電予備として良好に機能する金属カドミウムを含
み、利用率か向上されたアルカリ蓄電池用カドミウム負
極を容易に製造することかできる。On the other hand, according to another invention related to the present invention, by preparing a paste by blending metal cadmium obtained by a wet method in a wet state, the surface of metal cadmium in the paste is directly exposed to air. Since contact with metal cadmium can be avoided, formation of an oxide or hydroxide film on the surface of metal cadmium can be prevented. Therefore, by applying and drying the paste on an active material layer formed on a conductive substrate and containing cadmium oxide as an active material, metal cadmium can be maintained in a highly active state together with the active material. As a result, it is possible to easily produce a cadmium negative electrode for an alkaline storage battery, which contains metal cadmium that functions well as a discharge reserve without impeding the conductivity of the living material, and which has an improved utilization rate.
(実施例) 以下、本発明の実施例を詳細に説明する。(Example) Examples of the present invention will be described in detail below.
実施例1
湿式法によって得られた溶液中の金属カドミウム粉末を
吸引濾過により含水率30重量%に調製した。この含水
率の調製は、漏斗の大きさ及び吸引時間を調節して行な
った。得られた含水率30重量9oの金属カドミウム1
0重量部を酸化カドミウム90重量部、カーボニルニッ
ケル5重量部、カルボキシメチルセルロース 0.5重
量部、及びアクリル短繊維0.5重量部と共に分散混合
して水溶媒のベストを調製した。このペーストを導電性
支持体であるパンチトメタルに塗布し、120℃で2時
間乾燥させてカドミウム負極を製造した。Example 1 Metal cadmium powder in a solution obtained by a wet method was adjusted to have a moisture content of 30% by weight by suction filtration. The moisture content was adjusted by adjusting the size of the funnel and the suction time. The resulting metal cadmium 1 with a water content of 30 and a weight of 9o
A water solvent vest was prepared by dispersing and mixing 0 parts by weight with 90 parts by weight of cadmium oxide, 5 parts by weight of carbonyl nickel, 0.5 parts by weight of carboxymethyl cellulose, and 0.5 parts by weight of acrylic short fibers. This paste was applied to a conductive support, ie, punched metal, and dried at 120° C. for 2 hours to produce a cadmium negative electrode.
実施例2
酸化カドミウム、カーボニルニッケル、及びアクリル短
繊維をカルボキシメチルセルロースを含むエチレングリ
コール溶液に加えて第1のペーストを調製した。このペ
ーストをパンチトメタルに塗布し、120℃で2時間乾
燥させて活物質層を形成した。つづいて、実施例1と同
様に調製した含水率30重量%の金属カドミウム 10
0重量部をポリビニルアルコール0.5重量部及びカル
ボキシメチルセルロース0.5重量部を含む水溶液に加
えて第2のペーストを調製した。この第2のペーストを
前記活物質層に塗布し、120℃で2時間乾燥させてカ
ドミウム負極を製造した。Example 2 A first paste was prepared by adding cadmium oxide, carbonyl nickel, and short acrylic fibers to an ethylene glycol solution containing carboxymethyl cellulose. This paste was applied to punched metal and dried at 120° C. for 2 hours to form an active material layer. Next, metal cadmium 10 with a water content of 30% by weight prepared in the same manner as in Example 1.
A second paste was prepared by adding 0 parts by weight to an aqueous solution containing 0.5 parts by weight of polyvinyl alcohol and 0.5 parts by weight of carboxymethylcellulose. This second paste was applied to the active material layer and dried at 120° C. for 2 hours to produce a cadmium negative electrode.
比較例1 湿式法で得られた金属カドミウム粉末を水洗。Comparative example 1 Metal cadmium powder obtained by wet method is washed with water.
乾燥し、この金属カドミウムを用いて実施例1と同様な
組成のペーストを調製した以外、同実施例1と同様にし
てカドミウム負極を製造した。A cadmium negative electrode was produced in the same manner as in Example 1, except that a paste having the same composition as in Example 1 was prepared using this metal cadmium.
比較例2
乾式法で得られた金属カドミウム粉末を用いて実施例1
と同様な組成のペーストを調製した以外、同実施例1と
同様にしてカドミウム負極を製造した。Comparative Example 2 Example 1 using metal cadmium powder obtained by dry method
A cadmium negative electrode was produced in the same manner as in Example 1, except that a paste having the same composition as in Example 1 was prepared.
比較例3
比較例1と同様な方法により電極を製造した後、この電
極表面にニッケルメッキ処理を施して二・ソケルメッキ
処理カドミウム負極を製造した。なお、前記ニッケルメ
ッキ処理では硫酸ニッケルや塩化ニッケルなどを主とす
る市販の電解メ・ツキ用ワ・ソト浴中、30℃の温度下
、ニッケルを対極とした100mA/cmFの電流密度
で、1分間の電気メ・ツキを行なった後、水洗、乾燥す
る方法を採用した。Comparative Example 3 After producing an electrode in the same manner as in Comparative Example 1, the surface of the electrode was subjected to nickel plating to produce a di-Sokel plated cadmium negative electrode. In the nickel plating process, nickel was plated at a current density of 100 mA/cmF with nickel as the counter electrode at a temperature of 30°C in a commercially available bath for electrolytic metal plating mainly containing nickel sulfate or nickel chloride. A method was adopted in which the parts were heated with electricity for a few minutes, then washed with water and dried.
実施例1,2及び比較例1〜3のカドミウム負極を、公
知のペースト式ニッケル正極と組合わせて公称容量50
0+nAhの5種の蓄電池型試験セルを組立てた。この
5種の試験セルについて、20℃の温度下で2Cの電流
で一定時間充電し、つづいて、ICの電流で放電した。The cadmium negative electrodes of Examples 1 and 2 and Comparative Examples 1 to 3 were combined with a known paste-type nickel positive electrode to achieve a nominal capacity of 50
Five types of battery type test cells of 0+nAh were assembled. These five types of test cells were charged at a temperature of 20° C. with a current of 2 C for a certain period of time, and then discharged with an IC current.
このときの各試験セルの内圧をそれぞれ測定した。その
結果を第1図に示す。At this time, the internal pressure of each test cell was measured. The results are shown in FIG.
第1図から明らかなように各試験セルは、30分間の充
電により満充電となって内圧が上昇する。As is clear from FIG. 1, each test cell becomes fully charged after 30 minutes of charging, and the internal pressure increases.
この満充電後の実施例1.2及び比較例3の試験セルは
、比較例1.2の電池と比べて内圧上昇が小さいのかわ
かる。この原因は、実施例1,2及び比較例3のカドミ
ウム負極が、比較例1.2のカドミウム負極に比べて電
極内部における金属カドミウムの導電性が良好で利用率
か高いため、正極から発生する酸素ガスを多く消費(吸
収)していることによる。なお、比較例3の試験セルは
、負極表面のニッケルにより該負極の水素発生過電圧値
が低下するため充電時に少量の水素が発生し、この水素
が放電終了後も内部に残存した。It can be seen that the test cells of Example 1.2 and Comparative Example 3 after being fully charged have a smaller increase in internal pressure than the battery of Comparative Example 1.2. The reason for this is that the cadmium negative electrodes of Examples 1 and 2 and Comparative Example 3 have better conductivity and higher utilization rate of metal cadmium inside the electrodes than the cadmium negative electrodes of Comparative Example 1.2. This is due to consuming (absorbing) a large amount of oxygen gas. In the test cell of Comparative Example 3, a small amount of hydrogen was generated during charging because the nickel on the surface of the negative electrode lowered the hydrogen generation overvoltage value of the negative electrode, and this hydrogen remained inside even after the discharge was completed.
実施例3
湿式法によって得られた溶液中の金属カドミウム粉末を
吸引濾過して実施例1と同様の方法で含水率を調製し、
含水率が2.5,20,50,70,100重量%の金
属カドミウムをそれぞれ得た。得られた金属カドミウム
をそれぞれ用いて実施例1と同様にしてペーストの調製
及びパンチトメタルへの塗布。Example 3 The metal cadmium powder in the solution obtained by the wet method was suction-filtered to adjust the water content in the same manner as in Example 1,
Metallic cadmium having a water content of 2.5, 20, 50, 70, and 100% by weight was obtained, respectively. A paste was prepared and applied to punched metal in the same manner as in Example 1 using each of the obtained cadmium metals.
乾燥を行なうことにより6種のカドミウム負極を製造し
た。Six types of cadmium negative electrodes were manufactured by drying.
得られた各カドミウム負極を、公知のペースト式ニッケ
ル正極とそれぞれ組合わせて6種の蓄電池を組立てた。Six types of storage batteries were assembled by combining each of the obtained cadmium negative electrodes with a known paste-type nickel positive electrode.
各蓄電池について、0.ICの電流で15時間充電した
後、ICの電流で放電したときの放電容量を測定し、負
極の理論容量に対する前記711]定値の割合を利用率
として求めた。その結果を第2図に示す。For each storage battery, 0. After charging with the IC current for 15 hours, the discharge capacity when discharging with the IC current was measured, and the ratio of the above-mentioned 711] constant value to the theoretical capacity of the negative electrode was determined as the utilization rate. The results are shown in FIG.
第2図から明らかなように利用率の向上化の観点から、
含水率が5重量%以上の金属カドミウムを用いるのか望
ましいことがわかる。なお、含水率が70重fit 0
6を越える金属カドミウムを用いた場合、ペーストの粘
性か低下してパンチトメタルへの塗布か困難となった。As is clear from Figure 2, from the perspective of improving the utilization rate,
It can be seen that it is desirable to use metal cadmium with a water content of 5% by weight or more. In addition, the moisture content is 70% fit 0
When metallic cadmium exceeding 6 was used, the viscosity of the paste decreased and it became difficult to apply it to punched metal.
[発明の効果]
以上詳述した如く、本発明によれば利用率か向上して充
電時の酸素ガス吸収性能などに優れたアルカリ蓄電池用
カドミウム負極を容易に製造し得る方法を提供すること
ができる。[Effects of the Invention] As detailed above, according to the present invention, it is possible to provide a method for easily producing a cadmium negative electrode for an alkaline storage battery that has improved utilization rate and excellent oxygen gas absorption performance during charging. can.
第1図は実施例1,2及び比較例1〜3の試験セルにお
ける充放電時の内圧の変化を示す特性図、第2図は実施
例3の各蓄電池における負極製造に用いた金属カドミウ
ムの含水率に対する負極の利用率の変化を示す特性図で
ある。
出願人代理人 弁理士 鈴江武彦Figure 1 is a characteristic diagram showing changes in internal pressure during charging and discharging in the test cells of Examples 1 and 2 and Comparative Examples 1 to 3. FIG. 3 is a characteristic diagram showing a change in the utilization rate of the negative electrode with respect to the water content. Applicant's agent Patent attorney Takehiko Suzue
Claims (2)
式法により得られた金属カドミウムを湿潤状態で配合し
てペーストを調製する工程と、導電性基板上に前記ペー
ストを塗布、乾燥する工程とを具備することを特徴とす
るアルカリ蓄電池用カドミウム負極の製造法。(1) A step of preparing a paste by blending cadmium oxide as an active material and blending metallic cadmium obtained by a wet method in a wet state, and a step of applying the paste on a conductive substrate and drying it. A method for producing a cadmium negative electrode for an alkaline storage battery, comprising:
ペーストを調製する工程と、導電性基板上に前記ペース
トを塗布、乾燥して活物質層を形成する工程と、湿式法
により得られた金属カドミウムを湿潤状態で配合して第
2のペーストを調製する工程と、前記活物質層上に前記
第2のペーストを塗布、乾燥する工程とを具備すること
を特徴とするアルカリ蓄電池用カドミウム負極の製造法
。(2) A step of preparing a first paste by blending cadmium oxide as an active material, a step of applying the paste on a conductive substrate and drying it to form an active material layer, and a step of forming an active material layer by a wet method. A cadmium for alkaline storage battery comprising the steps of preparing a second paste by blending cadmium metal in a wet state, and applying and drying the second paste on the active material layer. Manufacturing method of negative electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2125373A JP2854926B2 (en) | 1990-05-17 | 1990-05-17 | Manufacturing method of cadmium negative electrode for alkaline storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2125373A JP2854926B2 (en) | 1990-05-17 | 1990-05-17 | Manufacturing method of cadmium negative electrode for alkaline storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0422065A true JPH0422065A (en) | 1992-01-27 |
| JP2854926B2 JP2854926B2 (en) | 1999-02-10 |
Family
ID=14908527
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2125373A Expired - Fee Related JP2854926B2 (en) | 1990-05-17 | 1990-05-17 | Manufacturing method of cadmium negative electrode for alkaline storage battery |
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| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012178296A (en) * | 2011-02-28 | 2012-09-13 | Sanyo Electric Co Ltd | Alkaline storage battery |
| CN114864877A (en) * | 2022-05-20 | 2022-08-05 | 湖北亿纬动力有限公司 | Preparation method and application of negative pole piece |
-
1990
- 1990-05-17 JP JP2125373A patent/JP2854926B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012178296A (en) * | 2011-02-28 | 2012-09-13 | Sanyo Electric Co Ltd | Alkaline storage battery |
| CN114864877A (en) * | 2022-05-20 | 2022-08-05 | 湖北亿纬动力有限公司 | Preparation method and application of negative pole piece |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2854926B2 (en) | 1999-02-10 |
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