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JP2002004095A - Insoluble anode and its power supply method - Google Patents

Insoluble anode and its power supply method

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Publication number
JP2002004095A
JP2002004095A JP2000185516A JP2000185516A JP2002004095A JP 2002004095 A JP2002004095 A JP 2002004095A JP 2000185516 A JP2000185516 A JP 2000185516A JP 2000185516 A JP2000185516 A JP 2000185516A JP 2002004095 A JP2002004095 A JP 2002004095A
Authority
JP
Japan
Prior art keywords
power supply
anode
electrode
insoluble
joined
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2000185516A
Other languages
Japanese (ja)
Inventor
Kazuhiro Kubota
一浩 久保田
Akira Kanno
章 管野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
AKAHOSHI KOGYO KK
Japan Carlit Co Ltd
Original Assignee
AKAHOSHI KOGYO KK
Japan Carlit Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by AKAHOSHI KOGYO KK, Japan Carlit Co Ltd filed Critical AKAHOSHI KOGYO KK
Priority to JP2000185516A priority Critical patent/JP2002004095A/en
Publication of JP2002004095A publication Critical patent/JP2002004095A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide insoluble anodes which are capable of manufacturing uniform metallic films at the same current density over the entire part of the electrode surfaces of the insoluble anodes and are uniform in the consumption of the electrode active surfaces without unevenness and a power feeding method for the same. SOLUTION: Constant currents are passed respectively independently from a plurality of power sources 4 to respective terminals 3 for anode power feeding, a plurality of which are joined to the cathode rear surface side of the insoluble anodes arranged at specified intervals along the curved surface of a cylindrical cathode in such a manner that the entire part of the electrode surfaces attains the same current density.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、高電流電解による連続
メッキ、金属箔製造等に使用される不溶性陽極及びその
給電方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an insoluble anode used for continuous plating by high current electrolysis, production of metal foil, and the like, and a power supply method thereof.

【0002】[0002]

【従来の技術】電解による連続メッキ分野や電解による
金属箔製造分野においては、技術の進歩により、極間距
離の短縮化、高速化、高電流密度化が進んでいる。その
一方、金属箔の製造においては、より厳しい金属箔の均
一性及び薄膜化が要求されている。
2. Description of the Related Art In the field of continuous plating by electrolysis and in the field of metal foil production by electrolysis, reductions in the distance between electrodes, higher speed, and higher current density are progressing due to technological advances. On the other hand, in the production of metal foil, stricter uniformity and thinner metal foil are required.

【0003】一般に、電解による連続金属箔製造装置で
は、円筒状陰極とその曲面に沿って一定間隔に配置され
た陽極との間に、金属イオンを含有する電解液を流して
電解させることにより、陰極表面に金属箔を析出させる
方法がとられているが、電解液出口では、電解液入口に
比べ、金属イオン濃度が低下するため、同一陽極におい
て、電流密度分布が生じてしまうため、均一な金属箔を
形成することができないと共に、陽極の電極活性面の消
耗も不均一となってしまうという問題点を有している。
また、エッヂ効果により、陽極周縁部に電流密度が集中
してしまうため、陽極周縁付近の金属箔が厚くなってし
まうと共に、陽極周縁部の電極活性面の消耗が大きくな
ってしまうという問題点も有している。。
In general, in a continuous metal foil producing apparatus by electrolysis, an electrolytic solution containing metal ions is caused to flow between a cylindrical cathode and an anode arranged at regular intervals along a curved surface of the cylindrical cathode to perform electrolysis. Although a method of depositing a metal foil on the cathode surface has been adopted, since the metal ion concentration is lower at the electrolyte outlet than at the electrolyte inlet, a current density distribution occurs at the same anode, so that a uniform There is a problem that the metal foil cannot be formed, and the consumption of the electrode active surface of the anode becomes non-uniform.
In addition, since the current density is concentrated on the peripheral edge of the anode due to the edge effect, the thickness of the metal foil near the peripheral edge of the anode increases, and the consumption of the electrode active surface of the peripheral edge of the anode increases. Have. .

【0004】上記問題点を解決するため、特開平5−2
22591号公報には、電極基体上に線材状の不溶性金
属電極を配置させて、電流密度が集中する部分には線状
不溶性金属電極の間隔を密にし、電流密度が小さな部分
には線状不溶性金属電極の間隔を疎とする電解用電極が
開示されている。また、特開平7−41980号公報に
は、電極基体表面に開口を有する不溶性金属電極が配置
され、かつ電流密度に応じて開口率を変えた不溶性金属
電極が配置された電解用電極が開示されている。
In order to solve the above problems, Japanese Patent Laid-Open Publication No.
Japanese Patent No. 225991 discloses that a linear insoluble metal electrode is arranged on an electrode substrate, the interval between the linear insoluble metal electrodes is increased in a portion where the current density is concentrated, and the linear insoluble metal electrode is arranged in a portion where the current density is small. An electrode for electrolysis in which the distance between metal electrodes is made small is disclosed. Japanese Patent Application Laid-Open No. 7-41980 discloses an electrode for electrolysis in which an insoluble metal electrode having an opening on the surface of an electrode substrate and an insoluble metal electrode whose opening ratio is changed according to current density are arranged. ing.

【0005】しかしながら、これらの方法は、電流密度
の均一化について、ある程度の対応は可能であるが、電
流密度分布が予想できない新規の装置、運転条件の変
化、あるいは金属箔の形成具合より運転条件にフィード
バックさせる場合等には、不十分であり、解決すべき点
が残っていた。
[0005] However, these methods can cope with uniformity of the current density to some extent, but are not suitable for a new apparatus in which the current density distribution cannot be predicted, a change in the operation condition, or an operation condition due to the formation condition of the metal foil. In the case where feedback is given to a group, it is insufficient and there are still points to be resolved.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、電極
面の各部を最適の電流密度に自由に制御させることによ
り、ムラがなく均一な厚さの金属箔を得ることができ、
かつ電極活性面が不均一に消耗しない不溶性陽極及びそ
の給電方法を提供することである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a metal foil having a uniform thickness without unevenness by freely controlling each part of an electrode surface to an optimum current density.
Another object of the present invention is to provide an insoluble anode in which an electrode active surface is not consumed unevenly and a power supply method therefor.

【0007】[0007]

【課題を解決するための手段】本発明者は、鋭意検討し
た結果、不溶性陽極の陰極裏面側に複数個の陽極給電用
ターミナルを接合させ、該陽極給電用ターミナルの各々
に対して、複数個の電源により、各々独立して、定電流
を通電させることにより、上記課題が解決し得ることを
見出し、本発明を完成するに至った。
As a result of intensive studies, the present inventors have joined a plurality of anode power supply terminals to the cathode back side of the insoluble anode, and provided a plurality of anode power supply terminals to each of the anode power supply terminals. It has been found that the above-mentioned problems can be solved by supplying a constant current to each of the power supplies independently, and the present invention has been completed.

【0008】すなわち、本発明は、円筒状陰極の曲面に
沿って一定間隔に配置させた不溶性陽極において、陽極
給電用ターミナルが、不溶性陽極の陰極裏面側に複数個
接合されてなることを特徴とする不溶性陽極であり、ま
た、本発明は、円筒状陰極の曲面に沿って一定間隔に配
置させた不溶性陽極の陰極裏面側に複数個接合された陽
極給電用ターミナルの各々に対して、複数の電源より、
各々独立して、定電流を通電させることを特徴とする給
電方法である。
That is, the present invention is characterized in that, in an insoluble anode arranged at regular intervals along the curved surface of a cylindrical cathode, a plurality of anode power supply terminals are joined to the cathode back side of the insoluble anode. The present invention also provides a plurality of anode power supply terminals joined to a plurality of insoluble anodes arranged on the cathode back side arranged at regular intervals along the curved surface of the cylindrical cathode. From the power supply
This is a power supply method characterized by supplying a constant current independently.

【0009】以下、本発明を、図1を参照して詳細に説
明する。
Hereinafter, the present invention will be described in detail with reference to FIG.

【0010】図1は、本発明の不溶性陽極の概略を示す
模式図の一例である。なお、本発明は、図1によりなん
ら限定されない。
FIG. 1 is an example of a schematic view showing the outline of the insoluble anode of the present invention. In addition, this invention is not limited at all by FIG.

【0011】図1は、円筒状陰極の曲面形状に合わせて
加工された電極活性面1を有する電極基体2からなる不
溶性陽極の陰極裏面側に複数個の陽極給電用ターミナル
3を接合させ、配線5によリ、複数個の電源4と陽極給
電用ターミナル3とが各々独立して接続されている様子
を示している。
FIG. 1 shows a structure in which a plurality of anode power supply terminals 3 are joined to the back surface side of a cathode of an insoluble anode composed of an electrode base 2 having an electrode active surface 1 processed in accordance with the curved surface shape of a cylindrical cathode. 5 shows that the plurality of power supplies 4 and the anode power supply terminals 3 are independently connected.

【0012】本発明の不溶性陽極は、以下の方法により
作製される。
The insoluble anode of the present invention is produced by the following method.

【0013】まず、円筒状陰極の曲面形状に合わせて加
工されたバルブ金属からなる電極基体2の陰極裏面側
に、同じくバルブ金属からなる陽極給電用ターミナル3
を複数個接合させる。
First, an anode power supply terminal 3 also made of a valve metal is placed on the back side of the cathode of an electrode base 2 made of a valve metal processed according to the curved surface shape of a cylindrical cathode.
Are joined together.

【0014】電極基体2及び陽極給電用ターミナル3と
して用いられるバルブ金属としては、チタン、ニオブ、
タンタル、ジルコニウム等があげられるが、チタンが安
価で加工しやすく好ましい。
The valve metals used as the electrode substrate 2 and the anode power supply terminal 3 include titanium, niobium, and the like.
Tantalum, zirconium and the like can be mentioned, and titanium is preferable because it is inexpensive and easy to process.

【0015】陽極給電用ターミナル3は、溶接またはネ
ジ止めにより、電極基体2に接合される。
The anode power supply terminal 3 is joined to the electrode base 2 by welding or screwing.

【0016】ネジ止めの場合、予め電極基体2に雌ネジ
を、陽極給電用ターミナル3の電極基体2に取り付ける
部分に雄ネジを切っておき、電極基体2に陽極給電用タ
ーミナル3をねじ込むことにより接合させる。ネジ止め
による接合は、電極基体2の穴開けが面倒であり、ま
た、ねじ込み部分が緩んでしまい、接触抵抗が大きくな
る恐れがあるので、溶接による接合が好ましい。
In the case of screwing, a female screw is cut into the electrode base 2 in advance, and a male screw is cut into a portion of the anode power supply terminal 3 to be attached to the electrode base 2, and the anode power supply terminal 3 is screwed into the electrode base 2. Join. Joining by screwing is troublesome in drilling a hole in the electrode base 2, and the threaded portion may be loosened, increasing the contact resistance. Therefore, joining by welding is preferred.

【0017】陽極給電用ターミナル3は、電極面積0.
5〜5.0dm2当り1個の割合で、電極基体2に接合
される。電極面積0.5dm2未満の場合、陽極給電用
ターミナル3の数が非常に多くなり、経済的でない。ま
た、5.0dm2超の場合、電流密度分布の制御が不十
分となり、不都合である。
The anode power supply terminal 3 has an electrode area of 0.1 mm.
It is joined to the electrode base 2 at a rate of one piece per 5 to 5.0 dm 2 . When the electrode area is less than 0.5 dm 2 , the number of anode power supply terminals 3 is extremely large, which is not economical. If it exceeds 5.0 dm 2 , the control of the current density distribution becomes insufficient, which is inconvenient.

【0018】以上のようにして、複数個の陽極給電用タ
ーミナル3を電極基体2に接合させた後、電極基体2上
の陰極側には、白金族金属またはその酸化物の電極活性
層1を被覆させる。
After the plurality of anode power supply terminals 3 are joined to the electrode substrate 2 as described above, the electrode active layer 1 of a platinum group metal or its oxide is placed on the cathode side of the electrode substrate 2. Cover.

【0019】電極基体2上に被覆させる電極活性層1で
ある白金族金属またはその酸化物としては、白金、酸化
白金、タンタル、酸化タンタル、酸化イリジウム等、公
知のものがあげられる。電極活性層1の主成分として
は、酸化イリジウムが好ましく、白金、タンタル、パラ
ジウム、ルテニウムを含有させてもよい。
As the platinum group metal or its oxide as the electrode active layer 1 to be coated on the electrode substrate 2, there may be mentioned known ones such as platinum, platinum oxide, tantalum, tantalum oxide and iridium oxide. The main component of the electrode active layer 1 is preferably iridium oxide, and may contain platinum, tantalum, palladium, or ruthenium.

【0020】電極活性層1は、電極基体2上に、焼成法
等公知の方法を用いて、被覆され、本発明の不溶性陽極
が作製される。
The electrode active layer 1 is coated on the electrode substrate 2 by a known method such as a baking method, and the insoluble anode of the present invention is produced.

【0021】上記のようにして作製した不溶性陽極を、
連続銅箔製造装置等の電解設備に設置させた後、陽極給
電用ターミナル3と複数の電源4とは、配線5により、
各々独立して接続され、陽極給電用ターミナル3に対し
て、各々独立して、定電流を通電させて、運転される。
The insoluble anode produced as described above is
After being installed in an electrolytic facility such as a continuous copper foil manufacturing apparatus, the anode power supply terminal 3 and the plurality of power supplies 4
The anode power supply terminals 3 are independently connected to each other, and are operated by supplying a constant current to the anode power supply terminals 3 independently.

【0022】陽極給電用ターミナル3には、複数の電源
4より、各々独立して、定電流が通電されて、定電流制
御が行われるため、不溶性陽極の電極面全体の電流密度
を同一とすることができる。
A constant current is supplied to the anode power supply terminal 3 independently from the plurality of power supplies 4 to control the constant current, so that the current density over the entire electrode surface of the insoluble anode is the same. be able to.

【0023】また、電流密度の変化が少ない場合には、
陽極給電用ターミナル3をいくつかのブロックに分割さ
せ、各ブロックと電源とを、独立して接続させて、各ブ
ロック毎に独立して定電流を通電させる、ブロック分割
による定電流制御でも差支えない。
When the change in current density is small,
The anode power supply terminal 3 may be divided into several blocks, each block may be connected to a power source independently, and a constant current may be supplied independently for each block. .

【0024】上記給電方法によれば、不溶性陽極の電極
面全体が同一電流密度となり、均一な金属箔が製造でき
ると共に、不溶性陽極の電極活性面の消耗もムラなく均
一となる。また、効率よい運転が可能となり、低ランニ
ングコストで運転することができ、経済性にも優れてい
る。
According to the above-described power supply method, the entire electrode surface of the insoluble anode has the same current density, a uniform metal foil can be manufactured, and the consumption of the electrode active surface of the insoluble anode becomes uniform. In addition, efficient operation can be performed, operation can be performed at low running cost, and economic efficiency is excellent.

【0025】[0025]

【作用】連続金属箔製造装置は、円筒状陰極とその曲面
に沿って一定の間隔で配置された陽極の間に金属イオン
を含んだ電解液を流し、電解することにより、陰極表面
に金属箔を析出させるが、電解液出口では、電解液入口
に比べ、金属イオン濃度が低下するため、電解液入口付
近の電流密度が高くなり、電解液入口付近では金属箔が
厚く、電解液出口付近では金属箔が薄くなり、均一な金
属箔が得ることが困難であり、また、電流密度の高い部
分では、電極活性面の消耗が早く、電極活性面の消耗が
不均一となり、さらに、電極周縁部では、エッヂ効果に
より、電極中央部よりも電流密度が高くなるため、金属
箔が不均一となり、同時に電極活性面の消耗も不均一と
なってしまう。
The continuous metal foil manufacturing apparatus is capable of flowing an electrolytic solution containing metal ions between a cylindrical cathode and an anode arranged at a constant interval along the curved surface of the metal foil, and electrolyzing the metal foil on the cathode surface. At the electrolyte outlet, the metal ion concentration is lower than at the electrolyte inlet, so the current density near the electrolyte inlet is higher, the metal foil is thicker near the electrolyte inlet, and near the electrolyte outlet. The thin metal foil makes it difficult to obtain a uniform metal foil, and in areas where the current density is high, the electrode active surface is quickly consumed, and the electrode active surface is not uniformly consumed. In this case, the current density becomes higher than that of the central part of the electrode due to the edge effect, so that the metal foil becomes non-uniform, and at the same time, the consumption of the electrode active surface becomes non-uniform.

【0026】不溶性陽極の陰極裏面側に複数個の陽極給
電用ターミナル3が接合された不溶性陽極の各々に対し
て、複数の電源4より、各々独立して、定電流を通電さ
せる給電方法を用いて、電解を行った場合、電極面の各
々の部分に対して、最適な定電流制御が、独立して行わ
れるため、電流密度が高くなりやすい電解液入口や電極
周縁部と、電流密度の低くなりやすい電解液出口や電極
中央部とに対して、同一定電流が通電でき、電極面全体
の電流密度を同一とすることができるので、均一な金属
箔が製造できると共に電極活性面の消耗を均一とするこ
とができる。
A power supply method is used in which a plurality of power supplies 4 independently supply a constant current to each of the insoluble anodes having a plurality of anode power supply terminals 3 joined to the cathode back side of the insoluble anode. Therefore, when electrolysis is performed, the optimal constant current control is performed independently for each part of the electrode surface, so that the electrolyte inlet and the electrode periphery, where the current density tends to be high, and the current density The same constant current can be applied to the electrolyte outlet and the center of the electrode, which tend to be low, and the current density on the entire electrode surface can be the same, so that a uniform metal foil can be manufactured and the electrode active surface is consumed. Can be made uniform.

【0027】[0027]

【発明の実施の形態】本発明の実施の形態を、実施例に
基き詳細に説明する。なお、本発明はこれらの実施例に
なんら限定されない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described in detail based on examples. Note that the present invention is not limited to these Examples.

【0028】実施例1 電極基体2は、バルブ金属であるチタン板(厚さ20m
m)を、幅1.5mに切断し、1/4円筒状(直径2m
φ)に加工した後、凸面(陰極裏面)側に、チタン製の
陽極給電用ターミナル3を、電極面積3dm2当り1個
の割合で、溶接により接合させた。
Example 1 An electrode substrate 2 was made of a titanium plate (20 m thick) as a valve metal.
m) is cut to a width of 1.5 m and a quarter cylindrical shape (2 m in diameter)
After processing into φ), an anode power supply terminal 3 made of titanium was welded to the convex surface (cathode back surface) side at a rate of one per 3 dm 2 of electrode area.

【0029】上記電極基体を脱脂後、10%シュウ酸中
で、温度80℃で5時間浸漬させて、粗面化した。つい
で、イリジウム:タンタル=6:4(モル比)の塩化イ
リジウム及び塩化タンタルからなる塗布液を、電極基体
凹面(陰極面)側に塗布し、温度500℃で30分間焼
成した。この操作を20回繰り返して、不溶性陽極を作
製した。
After degreasing the above electrode substrate, it was immersed in 10% oxalic acid at a temperature of 80 ° C. for 5 hours to roughen the surface. Then, a coating solution comprising iridium chloride and tantalum chloride in a ratio of iridium: tantalum of 6: 4 (molar ratio) was applied to the concave side (cathode side) of the electrode substrate, and baked at a temperature of 500 ° C. for 30 minutes. This operation was repeated 20 times to produce an insoluble anode.

【0030】連続金属箔製造用電解装置の円筒状陰極の
下部の半分を取り囲むように、上記製作した不溶性陽極
を、電極間距離10mmで設置させ、陽極給電用ターミ
ナル3に対して、複数の電源から各々独立して、配線5
により接続し、各陽極給電用ターミナル3に通電する定
電流を、各々独立して制御できるようにした。
The insoluble anode prepared above was placed at a distance of 10 mm between the electrodes so as to surround the lower half of the cylindrical cathode of the electrolytic device for producing a continuous metal foil. Each independently from the wiring 5
And the constant current flowing through each anode power supply terminal 3 can be independently controlled.

【0031】上記電解装置に、硫酸銅200g/L及び
硫酸100g/Lからなる電解液を、電解槽下方から上
方に30cm/分の速度で、ポンプにより循環させ、電
解液温度50℃として、電流密度50A/dm2の定電
流電解を1000時間連続して行い、厚さ20μmの銅
箔を製造した。
An electrolytic solution consisting of 200 g / L of copper sulfate and 100 g / L of sulfuric acid was circulated from the lower part of the electrolytic cell to the upper part at a rate of 30 cm / min by a pump in the above-mentioned electrolytic apparatus. Constant current electrolysis at a density of 50 A / dm 2 was continuously performed for 1000 hours to produce a copper foil having a thickness of 20 μm.

【0032】製造された銅箔の厚さの誤差は、±1.0
%であった。また、不溶性陽極の電極活性層の厚さは、
ムラなく均一に減少していることが観察された。
The thickness error of the manufactured copper foil is ± 1.0.
%Met. Also, the thickness of the electrode active layer of the insoluble anode,
It was observed that it was uniformly reduced without unevenness.

【0033】比較例1 実施例1において、電極基体2の陰極裏面側の中央部の
みに、陽極給電用ターミナル3を1個溶接させた以外
は、実施例1に準じて、厚さ20μmの銅箔を製造し
た。
Comparative Example 1 A 20-μm thick copper was prepared in the same manner as in Example 1 except that one anode power supply terminal 3 was welded only to the center portion of the electrode substrate 2 on the cathode back side. A foil was produced.

【0034】電解液入口付近の銅箔と電解液出口付近の
銅箔との厚さの差は、約20%であり、電極中央部の銅
箔と周縁部の銅箔との厚さの差は、約15%であった。
また、不溶性陽極の電極活性層の厚さは、電解液入口部
分の方が電解液出口部分よりも、約10%以上減少して
いることが観察された。
The thickness difference between the copper foil near the electrolyte inlet and the copper foil near the electrolyte outlet is about 20%, and the difference between the thickness of the copper foil at the center of the electrode and the thickness of the copper foil at the periphery is about 20%. Was about 15%.
Further, it was observed that the thickness of the electrode active layer of the insoluble anode was reduced by about 10% or more at the electrolyte inlet portion than at the electrolyte outlet portion.

【0035】[0035]

【発明の効果】不溶性陽極の陰極裏面側に複数個の陽極
給電用ターミナル3が接合された不溶性陽極の各々に対
して、複数の電源4より、各々独立して、定電流を通電
させる給電方法を用いて、電解を行った場合、電極面の
各々の部分に対して、最適な定電流制御が独立して行わ
れるため、電流密度が高くなりやすい電解液入口や電極
周縁部と、電流密度の低くなりやすい電解液出口や電極
中央部とに対して、同一定電流が通電でき、電極面全体
の電流密度を同一とすることができるので、均一な金属
箔が製造できると共に電極活性面の消耗を均一とするこ
とができる。
A power supply method in which a plurality of power supplies 4 independently supply a constant current to each of the insoluble anodes having a plurality of anode power supply terminals 3 joined to the cathode back side of the insoluble anode. When the electrolysis is performed using an electrode, the optimal constant current control is performed independently for each part of the electrode surface, so that the electrolyte inlet and the electrode peripheral portion where the current density tends to be high, and the current density The same constant current can flow to the electrolyte outlet and the center of the electrode, which tend to be low, and the current density on the entire electrode surface can be the same. The wear can be made uniform.

【0036】また、電極活性層の消耗を均一とすること
ができるので、電極交換時期も延ばすことができ、非常
に経済的である。
Also, since the consumption of the electrode active layer can be made uniform, the electrode replacement time can be extended, which is very economical.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の不溶性陽極の概略を示す模式図の一例
である。
FIG. 1 is an example of a schematic view schematically showing an insoluble anode of the present invention.

【符号の説明】[Explanation of symbols]

1 電極活性層 2 電極基体 3 陽極給電用ターミナル 4 電源 5 配線 REFERENCE SIGNS LIST 1 electrode active layer 2 electrode substrate 3 anode power supply terminal 4 power supply 5 wiring

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 円筒状陰極の曲面に沿って一定間隔に配
置させた不溶性陽極において、陽極給電用ターミナル
が、不溶性陽極の陰極裏面側に複数個接合されてなるこ
とを特徴とする不溶性陽極。
1. An insoluble anode, comprising a plurality of insoluble anodes arranged at regular intervals along a curved surface of a cylindrical cathode, wherein a plurality of anode power supply terminals are joined to the cathode back side of the insoluble anode.
【請求項2】 陽極給電用ターミナルが、溶接またはネ
ジ止めで接合されることを特徴とする請求項1記載の不
溶性陽極。
2. The insoluble anode according to claim 1, wherein the anode power supply terminal is joined by welding or screwing.
【請求項3】 陽極給電用ターミナルが、電極面積0.
5〜5.0dm2当り1個の割合で接合されていること
を特徴とする請求項1記載の不溶性陽極。
3. An anode power supply terminal having an electrode area of 0.
2. The insoluble anode according to claim 1, wherein one is bonded at a rate of 5 to 5.0 dm < 2 >.
【請求項4】 円筒状陰極の曲面に沿って一定間隔に配
置させた不溶性陽極の陰極裏面側に複数個接合された陽
極給電用ターミナルの各々に対して、複数の電源によ
り、定電流を、各々独立して通電させることを特徴とす
る給電方法。
4. A constant current is supplied by a plurality of power supplies to each of a plurality of anode power supply terminals joined to the cathode back side of insoluble anodes arranged at regular intervals along the curved surface of the cylindrical cathode. A power supply method characterized in that power is supplied independently of each other.
【請求項5】 円筒状陰極の曲面に沿って一定間隔に配
置させた不溶性陽極の陰極裏面側に複数個接合された陽
極給電用ターミナルを少なくとも2ブロック以上に分割
させて、少なくとも2つ以上の電源により、定電流を、
各々独立して通電させることを特徴とする給電方法。
5. An anode power supply terminal joined to a plurality of insoluble anodes, which are arranged at regular intervals along the curved surface of a cylindrical cathode, and are joined to at least two blocks or more, are divided into at least two blocks or more. Depending on the power supply,
A power supply method characterized in that power is supplied independently of each other.
JP2000185516A 2000-06-21 2000-06-21 Insoluble anode and its power supply method Pending JP2002004095A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2002004095A true JP2002004095A (en) 2002-01-09

Family

ID=18685828

Family Applications (1)

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Country Status (1)

Country Link
JP (1) JP2002004095A (en)

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