JPH033754B2 - - Google Patents

Info

Publication number
JPH033754B2
JPH033754B2 JP61061781A JP6178186A JPH033754B2 JP H033754 B2 JPH033754 B2 JP H033754B2 JP 61061781 A JP61061781 A JP 61061781A JP 6178186 A JP6178186 A JP 6178186A JP H033754 B2 JPH033754 B2 JP H033754B2
Authority
JP
Japan
Prior art keywords
conductor
electrolytic cell
auxiliary
anode
cathode
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
Application number
JP61061781A
Other languages
Japanese (ja)
Other versions
JPS62218593A (en
Inventor
Kazuo Sato
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.)
Dowa Holdings Co Ltd
Original Assignee
Dowa Mining 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 Dowa Mining Co Ltd filed Critical Dowa Mining Co Ltd
Priority to JP6178186A priority Critical patent/JPS62218593A/en
Publication of JPS62218593A publication Critical patent/JPS62218593A/en
Publication of JPH033754B2 publication Critical patent/JPH033754B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Electrolytic Production Of Metals (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(イ) 技術分野 本発明は、槽上縁部に相対峙して一方に陽極側
導体を、また他方に陰極側導体を配設した電解槽
に複数の陽極板と陰極板とを交互に装架配列して
電解を行なう場合に、陰・陽極板間の電流分布を
改善した電解槽に関するものである。 (ロ) 従来技術 従来、電解製錬法における極板(アノード、カ
ソード)と該極板への通電用導体(ブスバー)と
の接続接触方法としては、Walker式や
Anaconda式等種々の方法が行なわれているが、
いずれもその接続個所はアノード、カソードとも
槽上縁部に設けられた導体と一個所の接触だけで
行なわれている。 即ち、電解における従来の接触方法は、例えば
第3図に示す如く、導体2aとの接触により各ア
ノード3の片側肩部(図では右端)から電流が入
り、電解槽1内の電解液を介して隣接する各カソ
ード4に電流が流れ、該カソード4の反対側肩部
(図では左端)と接触する導体2bより電流が出
て行く。 しかしながら、このように各極板3,4が相応
する導体2a又は2bと一個所だけの接触である
と、導体と極板の接触部に異物が混入したり酸化
被膜が形成されるなど何らかの要因で電気の通り
が悪くなり、場合によつては全く通電されない絶
縁状態の極板が生じることも少なくない。 極板の電流の通りが悪くなつたり絶縁状態とな
ると、電解槽内で極板間の電流分布に不均一を生
じ、その結果カソードへの電着量の不均一や電着
面の悪化、ひいては電流効率の低下及び電着物の
品質悪化をもたらし、電解製錬において非常に大
きな問題となつていた。 (ハ) 発明の開示 本発明は、このような問題を解決するために、
従来極板が導体と左右片側一個所で接触していた
ものを、同一極性の極板の左右反対側を補助導体
を介して互いに電気的に接続することによつて接
触個所を2個所とし、これにより極板間の電流分
布の改善を図るようにした新規な電解槽を提供す
るものである。 即ち、本発明は槽上縁部で相対峙して一方に陽
極側導体、他方に陰極側導体を配設した電解槽に
おいて、上記導体上に該導体と反対極性の極板を
装架すべき部分に電気絶縁体を介して補助導体を
載設し、該補助導体は相互に電気的に接続してな
る電解槽に関するものである。 以下、本発明による電解槽を詳述する。 本発明においては、電解槽1内に複数枚セツト
されている各アノード3、カソード4がそれぞれ
同一極性の導体2a又は2bとの接触のみなら
ず、反対極性の導体2b又は2a側でも該反対極
性の導体に対して絶縁5された補助導体6を該反
対極性導体上に載設し、この補助導体6上に極板
を載置し、しかも補助導体6どうしを相互に電気
的に接続するのである。 例えば第1〜2図に示すように、両導体2a及
び2b上に従来と同様に設けられている電気絶縁
体5の上に、更に同一極性の極板間距離をもつて
櫛板状に一体形成された長い導電性の補助導体6
a,6bを載設し、導体2と絶縁体5と補助導体
6とを三層のサンドイツチ型に構成することによ
り、各アノード3はその左右両側肩部が導体2a
と補助導体6上に接触装架され、また各カソード
4はその左右両側肩部が導体2bと補助導体6a
上に接触装架されるので、常に電流は各アノード
3の左右両側肩部から入り、各カソード4の左右
両側肩部から出て行く。 従つて、例えば各アノード3はその左右片側肩
部(図では左端)において全て電気絶縁体5上で
補助導体6bを介して互いに接続されているの
で、仮に一部のアノード3と導体2aとの間で接
触不良があつても、補助導体6b側から該不良ア
ノードに確実に電流が流れるので、該アノードに
対しても電解が続行されることとなる。このこと
は、カソード4の場合も同様である。 なお、補助導体6は図示のように各絶縁体5を
カバーする(ただし、補助導体6の中間部分では
絶縁体5を省略して反対極性の導体面から浮かせ
るようにしても差支えない)一枚の櫛板状に形成
しないで、各絶縁体5上毎に載設して各補助導体
どうしを電線で結んでもよく、さらに該補助導体
6は一方の極性の導体2a又は2b上に設けるの
みでもよいが、添付図の如く左右両方の導体2a
及び2b上に設けることによつて、より完全な電
流分布とすることができる。また、本発明は金属
の電解のほか、水溶液の電解等あらゆる電解に適
用することができることは勿論である。 (ニ) 実施例 電解槽の両極導体上に電気絶縁体を介して補助
導体を載設した第1〜2図の方法により、鉛電解
精製を行なつた。その結果、第3図のような従来
の電解槽による場合と比較して、次表のような極
めて良好な結果を得ることができた。 電解条件: 電解液 Pb濃度 100g/ 遊離酸濃度(H2SiF6) 80g/ 電流密度 143A/m2
(a) Technical field The present invention provides an electrolytic cell in which a plurality of anode plates and cathode plates are alternately installed in an electrolytic cell in which an anode-side conductor is disposed on one side and a cathode-side conductor is disposed on the other side facing toward the upper edge of the cell. This invention relates to an electrolytic cell that improves current distribution between cathode and anode plates when performing electrolysis in a stacked arrangement. (b) Prior art Conventionally, as a connection method between an electrode plate (anode, cathode) and a current-carrying conductor (bus bar) in the electrolytic smelting method, the Walker type or
Various methods such as the Anaconda method have been used, but
Both the anode and the cathode are connected to a conductor provided at the upper edge of the tank at only one point. That is, in the conventional contact method in electrolysis, as shown in FIG. 3, for example, current is applied from one shoulder of each anode 3 (the right end in the figure) through contact with the conductor 2a, and the current flows through the electrolyte in the electrolytic cell 1. A current flows through each adjacent cathode 4, and the current flows out from the conductor 2b that contacts the opposite shoulder (the left end in the figure) of the cathode 4. However, if each electrode plate 3, 4 is in contact with the corresponding conductor 2a or 2b at only one place, there may be some factors such as foreign matter getting into the contact area between the conductor and the electrode plate or an oxide film being formed. This impairs the conduction of electricity, and in some cases, it is not uncommon to have insulated plates that do not conduct electricity at all. If the current flow through the plates becomes poor or the plates become insulated, the current distribution between the plates in the electrolytic cell becomes uneven, resulting in uneven amounts of electrodeposition on the cathode, deterioration of the electrodeposited surface, and even worse. This has caused a decrease in current efficiency and a deterioration in the quality of electrodeposited materials, which has become a very big problem in electrolytic smelting. (c) Disclosure of the invention In order to solve such problems, the present invention
Conventionally, the electrode plates were in contact with the conductor at one point on each side of the left and right sides, but by electrically connecting the opposite left and right sides of the electrode plates of the same polarity to each other via an auxiliary conductor, the number of contact points is reduced to two. This provides a novel electrolytic cell in which the current distribution between the electrode plates is improved. That is, the present invention provides an electrolytic cell in which an anode-side conductor is placed on one side and a cathode-side conductor is placed on the other side facing each other at the upper edge of the cell, and a plate having a polarity opposite to that of the conductor is mounted on the conductor. This relates to an electrolytic cell in which an auxiliary conductor is mounted on the portion via an electrical insulator, and the auxiliary conductors are electrically connected to each other. Hereinafter, the electrolytic cell according to the present invention will be explained in detail. In the present invention, each of the anodes 3 and cathodes 4 set in plurality in the electrolytic cell 1 not only contacts with the conductor 2a or 2b of the same polarity, but also contacts the conductor 2b or 2a of the opposite polarity with the opposite polarity. An auxiliary conductor 6 insulated with respect to the conductor 5 is placed on the opposite polarity conductor, a polar plate is placed on this auxiliary conductor 6, and the auxiliary conductors 6 are electrically connected to each other. be. For example, as shown in FIGS. 1 and 2, on top of the electrical insulator 5 provided on both conductors 2a and 2b in the same manner as in the past, a comb plate-like structure is further formed with a distance between the plates of the same polarity. Formed long conductive auxiliary conductor 6
a, 6b, and the conductor 2, insulator 5, and auxiliary conductor 6 are configured in a three-layer sanderch type, so that each anode 3 has its left and right shoulders connected to the conductor 2a.
and the auxiliary conductor 6, and each cathode 4 has its left and right shoulders connected to the conductor 2b and the auxiliary conductor 6a.
Since the electrodes are mounted in contact with each other, current always enters from the left and right shoulder portions of each anode 3 and exits from the left and right shoulder portions of each cathode 4. Therefore, for example, since the anodes 3 are all connected to each other on the electric insulator 5 at their right and left shoulder portions (the left end in the figure) via the auxiliary conductor 6b, it is assumed that some of the anodes 3 and the conductor 2a Even if there is a poor contact between them, current will surely flow from the auxiliary conductor 6b side to the defective anode, so that electrolysis will continue for the anode as well. This also applies to the cathode 4. The auxiliary conductor 6 is a single sheet that covers each insulator 5 as shown in the figure (however, the insulator 5 may be omitted in the middle part of the auxiliary conductor 6 and floated from the conductor surface of the opposite polarity). Instead of being formed into a comb plate shape, the auxiliary conductors 6 may be placed on each insulator 5 and the auxiliary conductors may be connected to each other with electric wires.Furthermore, the auxiliary conductors 6 may be provided only on the conductor 2a or 2b of one polarity. However, as shown in the attached diagram, both the left and right conductors 2a
and 2b, a more complete current distribution can be achieved. Furthermore, it goes without saying that the present invention can be applied to all types of electrolysis such as electrolysis of aqueous solutions in addition to metal electrolysis. (D) Example Lead electrolytic refining was carried out by the method shown in FIGS. 1 and 2, in which an auxiliary conductor was placed on the bipolar conductors of an electrolytic cell via an electrical insulator. As a result, we were able to obtain extremely good results as shown in the following table, compared to the case using a conventional electrolytic cell as shown in FIG. Electrolysis conditions: Electrolyte Pb concentration 100g/Free acid concentration ( H2SiF6 ) 80g/Current density 143A/ m2

【表】 (ホ) 発明の効果 本発明の電解槽は以上のようにしてなり、電解
槽における陰・陽両極板の電流分布の均一性が従
来よりも格段に向上するので、電流効率の向上を
図ることができ、更に金属の電解製錬においては
電解生成物の品質向上も図ることができる等、構
成簡単・製作容易にして多大な効果を有する。
[Table] (E) Effects of the Invention The electrolytic cell of the present invention is constructed as described above, and the uniformity of current distribution between the anode and negative electrode plates in the electrolytic cell is significantly improved compared to the conventional one, resulting in improved current efficiency. Furthermore, in electrolytic smelting of metals, it is possible to improve the quality of electrolyzed products, and the structure is simple and easy to manufacture, which has great effects.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明による電解槽の一例を示す平面
図、第2図は第1図の一部の縦断正面図、第3図
は従来の電解槽の平面図である。 符号説明、1……電解槽体、2……導体(ブス
バー)、3……アノード、4……カソード、5…
…絶縁体、6……補助導体。
FIG. 1 is a plan view showing an example of an electrolytic cell according to the present invention, FIG. 2 is a longitudinal sectional front view of a part of FIG. 1, and FIG. 3 is a plan view of a conventional electrolytic cell. Description of symbols, 1... Electrolytic cell body, 2... Conductor (bus bar), 3... Anode, 4... Cathode, 5...
...Insulator, 6...Auxiliary conductor.

Claims (1)

【特許請求の範囲】[Claims] 1 槽の左右両上縁部で相対峙して一方に陽極側
導体、他方に陰極側導体を配設した電解槽におい
て、上記導体上に該導体と反対極性の極板を装架
すべき部分に電気絶縁体を介して補助導体を載設
し、該補助導体は同一極性の極板間距離をもつて
導電体により櫛板状に一体化されて相互に電気的
に接続されてなることを特徴とする電解槽。
1. In an electrolytic cell in which an anode conductor is placed on one side and a cathode conductor is placed on the other side facing each other at both the left and right upper edges of the cell, a portion where a plate of opposite polarity to the conductor is mounted on the conductor. An auxiliary conductor is mounted on the auxiliary conductor through an electrical insulator, and the auxiliary conductor is integrated into a comb plate shape by the conductor with a distance between plates of the same polarity and electrically connected to each other. Characteristic electrolytic cell.
JP6178186A 1986-03-19 1986-03-19 Electrolytic cell Granted JPS62218593A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6178186A JPS62218593A (en) 1986-03-19 1986-03-19 Electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6178186A JPS62218593A (en) 1986-03-19 1986-03-19 Electrolytic cell

Publications (2)

Publication Number Publication Date
JPS62218593A JPS62218593A (en) 1987-09-25
JPH033754B2 true JPH033754B2 (en) 1991-01-21

Family

ID=13180975

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6178186A Granted JPS62218593A (en) 1986-03-19 1986-03-19 Electrolytic cell

Country Status (1)

Country Link
JP (1) JPS62218593A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7337676B2 (en) * 2019-12-05 2023-09-04 アサヒプリテック株式会社 Metal electrolytic recovery equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS545390B2 (en) * 1972-06-08 1979-03-16
JPS55128597A (en) * 1979-03-26 1980-10-04 Sumitomo Metal Mining Co Ltd Prevention of increase in contact resistance at electrode contact in metal salt electrolytic bath

Also Published As

Publication number Publication date
JPS62218593A (en) 1987-09-25

Similar Documents

Publication Publication Date Title
GB1235570A (en) Electrolytic cells
US6342136B1 (en) Busbar construction for electrolytic cell
US8986521B2 (en) Contact bar for capping board
KR850003912A (en) Electrolytic Device for Aluminum Production
US7854825B2 (en) Symmetical double contact electro-winning
WO2004031452A1 (en) Collector bar providing discontinuous electrical connection to cathode block
US3994798A (en) Module electrode assembly for electrolytic cells
US4396483A (en) Arrangement of busbars for electrolytic reduction cells
US7223324B2 (en) Capping board with separating walls
US6045669A (en) Structure of electric contact of electrolytic cell
JPH033754B2 (en)
US745412A (en) Electrode.
CN215713424U (en) Integrally assembled bipolar diaphragm-free electrolysis device
CN206204439U (en) Split type pole plate bridging arrangement and the electrolytic cell with the structure
US3969216A (en) Flotation separation
JP2000104193A (en) How to short the electrolytic cell block
US1359716A (en) Ebhest a
US1555424A (en) luening
SU703605A1 (en) Current supply to electrolyzer electrodes
GB200838A (en) Improvements in electrodes for electrolytic cells
US10689772B2 (en) Components, assemblies and methods for distributing electrical current in an electrolytic cell
CN221480136U (en) Electroplating flying bar with negative electrodes independently controlled in group
CN110453250A (en) Electrolysis device
CN221094307U (en) Negative plate bottom plate connection structure
US4060474A (en) Electrolytic cell of the diaphragm type comprising a base made of an insulating material