JPH065618B2 - Method for producing paste type cadmium cathode plate - Google Patents
Method for producing paste type cadmium cathode plateInfo
- Publication number
- JPH065618B2 JPH065618B2 JP59060178A JP6017884A JPH065618B2 JP H065618 B2 JPH065618 B2 JP H065618B2 JP 59060178 A JP59060178 A JP 59060178A JP 6017884 A JP6017884 A JP 6017884A JP H065618 B2 JPH065618 B2 JP H065618B2
- Authority
- JP
- Japan
- Prior art keywords
- active material
- transfer roller
- paste
- slurry
- cathode plate
- 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
- 229910052793 cadmium Inorganic materials 0.000 title claims description 19
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 title claims description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000011149 active material Substances 0.000 claims description 42
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 34
- 229910052799 carbon Inorganic materials 0.000 claims description 29
- 239000002002 slurry Substances 0.000 claims description 25
- 238000001035 drying Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 5
- 229940065285 cadmium compound Drugs 0.000 claims description 4
- 150000001662 cadmium compounds Chemical class 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 3
- 239000010409 thin film Substances 0.000 description 17
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 10
- 229910001882 dioxygen Inorganic materials 0.000 description 10
- 239000000843 powder Substances 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 7
- 239000011230 binding agent Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000004080 punching Methods 0.000 description 3
- 239000012779 reinforcing material Substances 0.000 description 3
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 2
- CXKCTMHTOKXKQT-UHFFFAOYSA-N cadmium oxide Inorganic materials [Cd]=O CXKCTMHTOKXKQT-UHFFFAOYSA-N 0.000 description 2
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 2
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 2
- 238000010422 painting Methods 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003860 storage 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
- H01M4/04—Processes of manufacture in general
- H01M4/0438—Processes of manufacture in general by electrochemical processing
- H01M4/044—Activating, forming or electrochemical attack of the supporting material
- H01M4/0445—Forming after manufacture of the electrode, e.g. first charge, cycling
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/34—Gastight accumulators
-
- 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
- H01M4/246—Cadmium electrodes
-
- 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
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
-
- 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
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
-
- 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
- H01M4/66—Selection of materials
- H01M4/665—Composites
- H01M4/667—Composites in the form of layers, e.g. coatings
-
- 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
- H01M4/72—Grids
- H01M4/74—Meshes or woven material; Expanded metal
- H01M4/742—Meshes or woven material; Expanded metal perforated material
-
- 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
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/027—Negative electrodes
-
- 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
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
-
- 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
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
-
- 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
- H01M4/72—Grids
- H01M4/74—Meshes or woven material; Expanded metal
-
- 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)
- Composite Materials (AREA)
- Materials Engineering (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は活物質の脱落が防止されると共に高率放電特性
が優れ、酸素ガス吸収性能が大幅に改良されたペースト
式カドミウム陰極板の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a paste type cadmium cathode plate in which the active material is prevented from falling off, the high rate discharge characteristics are excellent, and the oxygen gas absorption performance is significantly improved. It relates to a manufacturing method.
(ロ) 従来技術 従来、ニッケル−カドミウム電池の様なアルカリ蓄電池
に用いられるペースト式カドミウム陰極板は、特開昭5
8−80265号公報に示される様に予備充電量の一部
に相当する金属カドミウムと、主活物質である酸化カド
ミウムからなる活物質粉末にバインダーとしてのヒドロ
キシプロピルセルロース等の糊料及び補強材としてのポ
リプロピレン繊維等を加えて作製されたペーストを、パ
ンチングメタルの両面に塗着、乾燥して製造されてお
り、糊料に加えて添加された補強材としての繊維によっ
て極板強度の増加及びガス吸収性能の向上を行なってい
る。(B) Prior art Conventionally, a paste type cadmium cathode plate used for an alkaline storage battery such as a nickel-cadmium battery has been disclosed in Japanese Patent Laid-Open No.
As disclosed in Japanese Unexamined Patent Publication No. 8-80265, metal cadmium corresponding to a part of the precharge amount and active material powder composed of cadmium oxide which is a main active material are used as a binder such as hydroxypropyl cellulose as a binder and a reinforcing material. It is manufactured by applying a paste made by adding polypropylene fiber, etc. on both sides of a punching metal and drying it, and the fiber as a reinforcing material added in addition to the paste increases the plate strength and gas. The absorption performance is improved.
しかしながら、前述のように糊料に加え補強材としての
繊維を加えて極板を構成しても極板表面部の活物質粉末
の脱落を防止することはできず、極板容量の減少が起こ
ると共に作業環境が悪化するという問題点がある。一般
にバインダーとしての糊料の添加量を増加することによ
って活物質の保持力を大きくし極板強度を増すこともで
きるが、この場合糊料の増加は活物質粒子間の粒子伝導
性を劣化させることになるため、その添加量には限界が
あり、活物質粉末の脱落はある程度避けられないもので
あった。However, as described above, even if the electrode plate is formed by adding the fiber as the reinforcing material in addition to the paste, it is not possible to prevent the active material powder on the surface of the electrode plate from falling off, and the electrode plate capacity decreases. At the same time, there is a problem that the work environment deteriorates. Generally, it is possible to increase the holding power of the active material and increase the electrode plate strength by increasing the addition amount of the paste as a binder, but in this case, the increase of the paste deteriorates the particle conductivity between the active material particles. Therefore, there is a limit to the amount of addition, and it is unavoidable that the active material powder falls off to some extent.
また、ペースト式陰極板は焼結式極板のように活物質層
内に焼結金属による導電マトリックスを持たず、その活
物質層の主成分である酸化カドミウムの電子伝導性が低
いため、充電の際に生成する金属カドミウムは導電性芯
体の付近に偏在し、過充電によって陽極から発生する酸
素ガスと接触し易い陰極板表面に金属カドミウムが生成
され難いので、金属カドミウムと酸素ガスとが反応する
ことにより酸素ガスを消失させる酸素ガス吸収性能が劣
るという問題点があった。In addition, unlike the sintered electrode plate, the paste cathode plate does not have a conductive matrix of sintered metal in the active material layer, and cadmium oxide, which is the main component of the active material layer, has a low electronic conductivity, so charging is not possible. Metal cadmium generated at the time is unevenly distributed in the vicinity of the conductive core, and metal cadmium is difficult to be generated on the surface of the cathode plate which is easily contacted with oxygen gas generated from the anode due to overcharge, so that metal cadmium and oxygen gas There has been a problem that the oxygen gas absorption performance for eliminating oxygen gas by the reaction is poor.
(ハ) 発明の目的 本発明はかかる点に鑑みカドミウム活物質層の表面に水
溶性糊料を用いてカーボン薄膜層を形成することで活物
質の脱落を防止し、且つ高率放電特性及び酸素ガス吸収
性能を向上させると共に、前記カーボン薄膜層の厚みの
偏り及び陰極端子への導出部となる極板の芯体露出部へ
のカーボン層形成を防止することで電池性能の劣化を防
ぐペースト式カドミウム陰極板の製造方法を提供せしめ
んとするものである。(C) Object of the present invention In view of such a point, the present invention prevents the active material from falling off by forming a carbon thin film layer on the surface of the cadmium active material layer by using a water-soluble paste, and has a high rate discharge characteristic and oxygen. A paste formula that improves gas absorption performance and prevents deterioration of battery performance by preventing unevenness in the thickness of the carbon thin film layer and formation of a carbon layer on the exposed portion of the core body of the electrode plate that is the lead-out portion to the cathode terminal. A method for manufacturing a cadmium cathode plate is provided.
(ニ) 発明の構成 本発明のペースト式カドミウム陰極板の製造方法は、パ
ンチングメタル等の導電性芯体の表面にカドミウム化合
物を主体とするペーストを塗着し、半乾燥状態の活物質
層を形成した後、少なくとも2個のローラーを連結して
なる転写ローラー群を用いて水溶性糊料溶液にカーボン
粉末が分散されたスラリーを、該スラリー液に部分的に
浸漬されているローラーから順次隣り合うローラーに転
写して行くことで最終的に厚みを調整して前記活物質層
表面に塗着し、その後本乾燥するものである。(D) Structure of the invention The method for producing a paste-type cadmium cathode plate of the present invention is a method in which a paste containing a cadmium compound as a main component is applied to the surface of a conductive core such as a punching metal to form a semi-dried active material layer. After being formed, a slurry in which carbon powder is dispersed in a water-soluble paste solution is sequentially used from a roller partially immersed in the slurry liquid by using a transfer roller group in which at least two rollers are connected to each other. The thickness of the active material layer is finally adjusted by transferring it to a matching roller, and is then applied to the surface of the active material layer, followed by main drying.
(ホ) 実 施 例 本発明の一実施例を第1図乃至第3図を用いて以下に説
明する。(E) Example An example of the present invention will be described below with reference to FIGS. 1 to 3.
第1図はペースト式カドミウム陰極板の製造装置の説明
図であり、この極板製造装置を用いることによりパンチ
ングメタルからなる帯状の導電性芯体(7)は巻き出しロ
ーラー(1)から導出されて巻き取りローラー(6)で巻き取
られる間に、活物質スラリー槽(2)を通過してカドミウ
ム化合物を主体とするスラリーが塗着され、該活物質ス
ラリー槽(2)の上方に位置するスリット(8)により塗着厚
みが調整された後、中間乾燥機(3)で乾燥されることに
より、まず導電性芯体の表面に活物質層が形成される。
次いでこの活物質層が表面に形成された導電性芯体は、
転写ローラー装置(4)を通過する間に水溶性糊料溶液に
カーボン粉末が均一に分散されたカーボンスラリーが活
物質層の表面のみに一定の厚みで塗着され、引き続いて
本乾燥機(5)によって乾燥されて、活物質層表面にカー
ボン薄膜層を有する完成極板となる。FIG. 1 is an explanatory view of a paste-type cadmium cathode plate manufacturing apparatus. By using this electrode plate manufacturing apparatus, a strip-shaped conductive core body (7) made of punching metal is led out from an unwinding roller (1). While being wound by the take-up roller (6), the slurry containing the cadmium compound as a main component is applied by passing through the active material slurry tank (2) and is located above the active material slurry tank (2). After the coating thickness is adjusted by the slits (8), the active material layer is first formed on the surface of the conductive core by being dried by the intermediate dryer (3).
Next, the conductive core having the active material layer formed on the surface is
While passing through the transfer roller device (4), the carbon slurry in which the carbon powder is uniformly dispersed in the water-soluble paste solution is applied to only the surface of the active material layer with a constant thickness, and then the main dryer (5 ), It becomes a completed electrode plate having a carbon thin film layer on the surface of the active material layer.
この製造方法では中間乾燥機(3)と本乾燥機(5)によって
2回に分けて乾燥が行なわれるので、中間乾燥機(3)で
は予め完全乾燥を行なう必要はなく、後の本乾燥機(5)
により充分に完全乾燥を行なうことが可能であるため、
中間乾燥機(3)では転写ローラー装置を通過する間に活
物質が装置のローラーに付着せず且つ活物質層にくずれ
が生じない程度に乾燥すれば充分である。また、この乾
燥によって得られた内部が多少湿った状態で、その外部
がある程度乾燥した状態の活物質層は、完全乾燥された
活物質層に比べて表面に塗着形成されるカーボン薄膜層
の結着性が良好であり、極板完成後にカーボン薄膜層の
脱落、剥離が起こり難い。In this manufacturing method, since the intermediate dryer (3) and the main dryer (5) perform drying in two steps, the intermediate dryer (3) does not need to be completely dried in advance, and the subsequent main dryer can be used. (Five)
Since it is possible to fully dry with
It is sufficient for the intermediate dryer (3) to dry the active material such that the active material does not adhere to the rollers of the apparatus and the active material layer does not collapse while passing through the transfer roller apparatus. In addition, the active material layer obtained by the drying in a state where the inside is slightly wet and the outside is dried to some extent has a carbon thin film layer formed by coating on the surface as compared with a completely dried active material layer. The binding property is good, and the carbon thin film layer is unlikely to fall off or peel off after the electrode plate is completed.
第2図及び第3図は転写ローラー装置の斜視図及び転写
ローラーと極板の接触状態を示す部分断面図であり、転
写ローラー装置は第2図に示す様に帯状極板(9)の各面
毎に配設された第1の転写ローラー(10)、第2の転写ロ
ーラー(11)及び第3の転写ローラー(12)からなる転写ロ
ーラー群と、この第2の転写ローラー(11)と第3の転写
ローラー(12)を夫々第1の転写ローラー(10)と平行を保
ったままスライドさせて各転写ローラー間の間隔を調整
するための長孔(13)(14)を有すると共にこれら転写ロー
ラー(10)(11)(12)を回転させる駆動部(15)と、水溶性糊
料にカーボン粉末が分散されてなるスラリー溶液を内部
に有するカーボンスラリー槽(16)とから構成されてお
り、前記スラリー溶液には第1の転写ローラー(10)が部
分的に浸漬されている。この転写ローラー装置では各転
写ローラー(10)(11)(12)を回転させることで、前記第1
の転写ローラー(10)の表面にカーボンスラリーが付着
し、この付着したカーボンスラリーは第1の転写ローラ
(10)と第2の転写ローラー(11)との間隙により厚みが調
整されると共に第2の転写ローラー(11)の表面に転写さ
れる。そして同様にして第2の転写ローラー(11)と第3
の転写ローラー(12)との間隙により最終的な厚みに調整
されて第3の転写ローラー(12)の表面に転写され、第3
の転写ローラー(12)から極板(9)の活物質層表面に装着
される。また、ここに於いて第3の転写ローラー(12)は
第3図に示す様に極板の活物質層(17)表面にのみ接触す
るため、導電性芯体(18)の露出部にはカーボン薄膜層は
形成されることはない。2 and 3 are a perspective view of the transfer roller device and a partial cross-sectional view showing a contact state between the transfer roller and the electrode plate. The transfer roller device is shown in FIG. A transfer roller group including a first transfer roller (10), a second transfer roller (11), and a third transfer roller (12) arranged on each surface, and the second transfer roller (11) The third transfer roller (12) has long holes (13) (14) for adjusting the distance between the transfer rollers by sliding the third transfer roller (12) in parallel with the first transfer roller (10). The transfer roller (10) (11) (12) to rotate the drive unit (15), and a carbon slurry tank (16) having a slurry solution containing carbon powder dispersed in a water-soluble paste The first transfer roller 10 is partially immersed in the slurry solution. In this transfer roller device, by rotating each transfer roller (10) (11) (12),
Carbon slurry adheres to the surface of the transfer roller (10) of the first transfer roller.
The thickness is adjusted by the gap between the (10) and the second transfer roller (11), and it is transferred onto the surface of the second transfer roller (11). Then, similarly, the second transfer roller (11) and the third
The final thickness is adjusted by the gap between the second transfer roller (12) and the third transfer roller (12) to be transferred to the surface of the third transfer roller (12).
The transfer roller (12) is attached to the surface of the active material layer of the electrode plate (9). Further, here, the third transfer roller (12) contacts only the surface of the active material layer (17) of the electrode plate as shown in FIG. 3, so that the exposed portion of the conductive core (18) is not exposed. No carbon thin film layer is formed.
したがって、転写ローラ装置によって装着するカーボン
スラリー量を活物質層表面に於いてむらなく一定にする
ことができるため、極板表面に電子伝導性が部分的に低
くなるところが生じることがなく、また、カーボンスラ
リーが結着し難い芯体露出部にカーボン薄膜層が形成さ
れることがないので、スプレーによってカーボンスラリ
ーを塗着する方法及び極板をカーボンスラリー中に通す
ることにより塗着する所謂ディッピングによってカーボ
ン薄膜層を形成した際に生じる芯体露出部からのカーボ
ン薄膜層の脱落、剥離による電池性能の劣化が生じるこ
とがない。Therefore, since the amount of carbon slurry to be mounted by the transfer roller device can be made uniform on the surface of the active material layer, there is no place where the electron conductivity is partially lowered on the surface of the electrode plate. Since the carbon thin film layer is not formed on the exposed portion of the core body where the carbon slurry is hard to bind, the method of applying the carbon slurry by spraying and the so-called dipping in which the electrode plate is passed through the carbon slurry Thus, the carbon thin film layer does not fall off from the exposed core portion when the carbon thin film layer is formed, and the deterioration of the battery performance due to peeling does not occur.
次いでカーボンスラリーとして純水、ヒドロキシプロピ
ルセルローズ、グラファイトを重量比で100:20:
2の割合で調整して作製した2000cps(at25
℃)の粘度を持つスラリー溶液を用いて、前述の極板製
造装置によって活物質層表面に厚さ約5ミクロンのカー
ボン薄膜層を有するペースト式カドミウム陰極板を作製
し、こうして作製された陰極板を所定寸法に切断して公
知のニッケル陽極板と組み合わせて公称容量1200m
AHのニッケル−カドミウム電池を得た。Then, as a carbon slurry, pure water, hydroxypropyl cellulose, and graphite were mixed in a weight ratio of 100: 20:
2000cps (at25
A paste type cadmium cathode plate having a carbon thin film layer having a thickness of about 5 μm on the surface of the active material layer is produced by the above-mentioned electrode plate producing apparatus using a slurry solution having a viscosity of (° C.). Is cut into a predetermined size and combined with a known nickel anode plate, the nominal capacity is 1200 m
An AH nickel-cadmium battery was obtained.
この本発明による製造方法を用いて作製したペースト式
陰極板は水溶性糊料によって表面の強度が増加している
ため活物質粉末及びカーボン粉末の脱落が全くない優れ
たものであった。これに対して導電性芯体に活物質を塗
着、乾燥して作製された従来の陰極板は、表面に手を触
れると活物質粉末が多数付着するため、電池組立工程等
に於いて脱落する活物質粉末により作業環境がそこなわ
れると共に脱落した活物質粉末により極板容量が減少す
るため極板容量にバラツキが生じるおそれがある。ま
た、本発明の陰極板を用いた電池は、従来の陰極板を用
いた電池に比し酸素ガス吸収性能及び高率放電特性が優
れていることがわかった。この理由を推測するに、酸素
ガス吸収性能が優れたのは、本発明の陰極板を用いた電
池では充電の際に導電性芯体付近から生成する電子伝導
性の良好な金属カドミウムが徐々に極板表面に向って分
布して行き、ある一部分で極板表面のカーボン薄膜層に
到達すると導電性芯体とカーボン薄膜層が電気的に接続
されたことになり電子伝導性の良好なカーボン薄膜層か
ら給電を受けて極板表面に金属カドミウムが多く生成す
るため、過充電時に陽極から発生する酸素ガスが陰極板
表面の金属カドミウムと反応して酸素ガスを吸収したか
らと考えられ、高率放電特性が優れたのは水溶性糊料が
アルカリ電解液と接することでゲル化して陰陽極板間に
保持される電解液量が増大したからと考えられ、放電状
態の電池内部抵抗を測定すると本発明による陰極板を用
いた電池は従来電池に比し低い値に抑えられていた。The paste-type cathode plate manufactured by the manufacturing method according to the present invention was excellent in that the active material powder and the carbon powder did not fall off because the surface strength was increased by the water-soluble paste. On the other hand, a conventional cathode plate made by applying an active material to the conductive core and drying it will drop a large amount of active material powder when the surface is touched, so it does not fall off during the battery assembly process. There is a possibility that the working environment will be impaired by the active material powder that is generated and that the electrode plate capacity will be reduced by the active material powder that has fallen off, so that there will be variations in the electrode plate capacity. It was also found that the battery using the cathode plate of the present invention is superior in oxygen gas absorption performance and high rate discharge characteristics to the battery using the conventional cathode plate. Inferring the reason for this, the oxygen gas absorption performance was excellent because in the battery using the cathode plate of the present invention, metal cadmium with good electron conductivity gradually generated from the vicinity of the conductive core during charging was gradually formed. When the carbon thin film is distributed toward the surface of the electrode plate and reaches a carbon thin film layer on the surface of the electrode plate at a certain part, it means that the conductive core and the carbon thin film layer are electrically connected, and thus the carbon thin film has good electron conductivity. It is considered that because a large amount of metal cadmium is generated on the surface of the electrode plate by receiving power from the layer, the oxygen gas generated from the anode during overcharge reacts with the metal cadmium on the surface of the cathode plate and absorbs oxygen gas. It is considered that the excellent discharge characteristics were due to the fact that the water-soluble paste gelled when it came into contact with the alkaline electrolyte and the amount of electrolyte retained between the cathode and anode plates increased, and when the internal resistance of the battery in a discharged state was measured. According to the invention Battery using the electrode plate was suppressed to a low value compared with conventional batteries.
尚、本発明の陰極板表面に形成されるカーボン薄膜層の
厚みはカーボンスラリー粘度に影響を及ぼすため、スラ
リーの温度管理が重要であることは云うまでもない。Needless to say, temperature control of the slurry is important because the thickness of the carbon thin film layer formed on the surface of the cathode plate of the present invention affects the viscosity of the carbon slurry.
(ヘ) 発明の効果 本発明のペースト式カドミウム陰極板は、導電性芯体の
表面にカドミウム化合物を主体とするペーストあるいは
スラリーの塗着して乾燥することにより活物質層を形成
した後、少なくとも2個のローラーからなる転写ローラ
ー群を用いて水溶性糊料溶液にカーボン粉末が分散され
たスラリーを、隣り合うローラーに順次転写して行くこ
とで厚みを調整して前記活物質層表面に塗着して乾燥す
るものであるから、活物質層表面に均一なカーボン薄膜
層を形成することができ、また、このカーボン薄膜層に
よって活物質粉末の脱落がなく、酸素ガス吸収性能及び
高率放電特性の良好なペースト式カドミウム陰極板を得
ることができる。(F) Effect of the invention The paste-type cadmium cathode plate of the present invention has at least after forming an active material layer by applying a paste or slurry mainly containing a cadmium compound on the surface of the conductive core and drying the active material layer. Using a transfer roller group consisting of two rollers, the slurry in which the carbon powder is dispersed in the water-soluble paste solution is sequentially transferred to the adjacent rollers to adjust the thickness and apply it to the surface of the active material layer. Since it is deposited and dried, it is possible to form a uniform carbon thin film layer on the surface of the active material layer, and the active material powder does not fall off due to this carbon thin film layer, and the oxygen gas absorption performance and high rate discharge can be achieved. A paste type cadmium cathode plate having good characteristics can be obtained.
第1図乃至第3図は本発明の一実施例にかかり、第1図
はペースト式カドミウム陰極板の製造装置の説明図、第
2図は転写ローラー装置の斜視図、第3図は転写ローラ
ーと極板の接触状態を示す断面図である。 (2)…活物質スラリー槽、(3)…中間乾燥機、(4)…転写
ローラー装置、(5)…本乾燥機、(7)…導電性芯体、(10)
…第1の転写ローラー、(11)…第2の転写ローラー、(1
2)…第3の転写ローラー、(16)…カーボンスラリー槽。1 to 3 relate to an embodiment of the present invention. FIG. 1 is an explanatory view of an apparatus for manufacturing a paste type cadmium cathode plate, FIG. 2 is a perspective view of a transfer roller device, and FIG. 3 is a transfer roller. It is sectional drawing which shows the contact state of an electrode plate. (2) ... Active material slurry tank, (3) ... Intermediate dryer, (4) ... Transfer roller device, (5) ... Main dryer, (7) ... Conductive core, (10)
… First transfer roller, (11)… Second transfer roller, (1
2) ... Third transfer roller, (16) ... Carbon slurry tank.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 酒井 洋志 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (72)発明者 原口 洋 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (56)参考文献 特開 昭53−86442(JP,A) 特開 昭54−93429(JP,A) 松谷守康著「増補塗装と塗装設備」(昭 45−11−20)技術書院P.96−97 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Hiroshi Sakai 2-18 Keihan Hondori, Moriguchi City, Osaka Sanyo Electric Co., Ltd. (72) Inventor Hiroshi Haraguchi 2-18 Keihan Hondori, Moriguchi City, Osaka Sanyo Denki Co., Ltd. (56) References JP-A-53-86442 (JP, A) JP-A-54-93429 (JP, A) Moriyasu Matsutani "Additional Painting and Painting Equipment" (Sho 45-11-20) Technical Institute P. 96-97
Claims (1)
体とするペーストあるいはスラリーを塗着して半乾燥状
態で活物質層を形成した後、水溶性糊料溶液にカーボン
粒子が分散されたスラリーを、少なくとも2個のローラ
ーからなる転写ローラー群を用いて隣り合うローラーに
順次転写して行くことで厚みを調整して前記活物質層表
面に塗着し、ついで本乾燥することを特徴とするペース
ト式カドミウム陰極板の製造方法。1. A paste or slurry mainly containing a cadmium compound is applied to the surface of a conductive core to form an active material layer in a semi-dried state, and then carbon particles are dispersed in a water-soluble paste solution. Characterized in that the slurry is applied to the surface of the active material layer by sequentially transferring the slurry to adjacent rollers using a transfer roller group consisting of at least two rollers, and then performing main drying. Method for manufacturing paste type cadmium cathode plate.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59060178A JPH065618B2 (en) | 1984-03-27 | 1984-03-27 | Method for producing paste type cadmium cathode plate |
| US06/680,817 US4614696A (en) | 1983-12-20 | 1984-12-12 | Negative electrode plate for alkaline storage cells of sealed type |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59060178A JPH065618B2 (en) | 1984-03-27 | 1984-03-27 | Method for producing paste type cadmium cathode plate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60202667A JPS60202667A (en) | 1985-10-14 |
| JPH065618B2 true JPH065618B2 (en) | 1994-01-19 |
Family
ID=13134637
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59060178A Expired - Lifetime JPH065618B2 (en) | 1983-12-20 | 1984-03-27 | Method for producing paste type cadmium cathode plate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH065618B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6870530B2 (en) * | 2017-08-11 | 2021-05-12 | トヨタ自動車株式会社 | Electrode plate manufacturing method |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5386442A (en) * | 1977-01-10 | 1978-07-29 | Matsushita Electric Industrial Co Ltd | Negative electrode for alkaline storage battery |
| JPS5493429A (en) * | 1978-09-08 | 1979-07-24 | Furukawa Battery Co Ltd | Method of producing plate for alkaline storage battery |
-
1984
- 1984-03-27 JP JP59060178A patent/JPH065618B2/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| 松谷守康著「増補塗装と塗装設備」(昭45−11−20)技術書院P.96−97 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60202667A (en) | 1985-10-14 |
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