JPS6058317B2 - Current flow gap adjustment device for assembly electrode support device of radial cell type electrolyzer - Google Patents
Current flow gap adjustment device for assembly electrode support device of radial cell type electrolyzerInfo
- Publication number
- JPS6058317B2 JPS6058317B2 JP3220782A JP3220782A JPS6058317B2 JP S6058317 B2 JPS6058317 B2 JP S6058317B2 JP 3220782 A JP3220782 A JP 3220782A JP 3220782 A JP3220782 A JP 3220782A JP S6058317 B2 JPS6058317 B2 JP S6058317B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- energizing
- electrode support
- drum
- bath
- 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
Links
- 239000002184 metal Substances 0.000 claims description 21
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 6
- 238000007654 immersion Methods 0.000 claims description 5
- 238000013519 translation Methods 0.000 claims description 5
- 239000003792 electrolyte Substances 0.000 claims 1
- 238000007747 plating Methods 0.000 description 10
- 230000007423 decrease Effects 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000005246 galvanizing Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
Landscapes
- Electroplating Methods And Accessories (AREA)
Description
【発明の詳細な説明】
この発明は、ラジアルセル型電解槽における組立て電
極支持装置の通電ギャップ調整装置に関し、とくに電解
液中における溶出などによる肉厚 の減少を補うべく、
逐次に更新される消耗電極片の、電解槽内における載置
保持と、更新の際の順送り移動の案内とを、電解のため
の大電流の伝導、導通下に司る電極サポートと、これに
載置した上記消耗電極片群とからなる組立て電極の電解
槽内における洛中懸垂姿勢を保持したまま、該電解槽内
で通電用回転ドラムに沿つて浴浸通板される、複処理金
属ストリップとの間の通電ギャップを、操業中、容易に
調節することを可能ならしめようとするものである。[Detailed Description of the Invention] The present invention relates to an energization gap adjustment device for an assembled electrode support device in a radial cell type electrolytic cell.
The consumable electrode pieces, which are to be replaced one after another, are kept in place in the electrolytic cell and guided to be moved sequentially during renewal. The assembled electrode consisting of the group of consumable electrode pieces placed in the electrolytic cell is kept in a suspended position in the electrolytic cell, and the multi-processed metal strip is passed through the bath along the energizing rotating drum in the electrolytic cell. The purpose is to make it possible to easily adjust the energization gap between the two during operation.
一般にラジアルセル型電解槽は、たとえば冷延薄板の
ような金属ストリップの連続亜鉛めつきラインのごとき
において、とくに高速下に、従つて著しく高能率の電解
操業に適合すべく、該槽内に、大外径の通電用回転ドラ
ムを、そのほぼ半周にわたつてめつき液中に浸漬し、槽
外のデフレクターロールを介して金属ストリップを電解
槽の内外に導入し、導出して浴浸通板させるように通電
用回転ドラムの外周に巻きがけ走行させ、そのJ間、通
電用回転ドラムに対しそのドラム自体の浸漬周面の2等
分領域にておのおの対をなし、該ドラムの半径方向に金
属ストリップとの間で均整な通電ギャップを隔てて向い
合う配置の陽極(アノード)からめつき液を通して大電
流の通電を行う;ように使用される。In general, radial cell electrolyzers are designed to be particularly suitable for high-speed and therefore highly efficient electrolysis operations, such as in continuous galvanizing lines for metal strips such as cold-rolled sheets. A rotating drum with a large outer diameter for energization is immersed in the plating solution over approximately half its circumference, and a metal strip is introduced into and out of the electrolytic tank via a deflector roll outside the tank, and then brought out to pass through the bath. During this time, the coils are wound around the outer periphery of the energizing rotating drum so that the energizing drum is immersed, and during that time, each pair is formed in a bisected area of the immersed circumferential surface of the energizing rotating drum, and in the radial direction of the drum. It is used to pass a large current through a plating solution from an anode that faces the metal strip with a uniform current-carrying gap in between.
この場合、金属ストリップの片面でのみ電解が行われ
るので、片面だけめつきを行つて他面を無処理のままと
するような、いわゆる片面めつきに有利に適合すること
も特色に数えられるが、この種の大規模施設にあつては
、甚しい大電力が、投入されるので、上記の通電ギャッ
プを、できる限り小さく維持することが、無効消費電力
を軽減抑制するためにも、肝要てある。In this case, since electrolysis is performed only on one side of the metal strip, it is also advantageous for so-called single-sided plating, where only one side is plated and the other side is left untreated. In this type of large-scale facility, an extremely large amount of power is input, so it is essential to keep the above-mentioned power supply gap as small as possible in order to reduce and control reactive power consumption. be.
ところで通常の電気めつきにあつては、アノードとして
不溶性電極を用いる場合、めつきをすべき金属を可溶性
電極に用いる場合とがあり、これらのうちとくに後者は
、めつき液の保守管理が、アノードから不断にめつき金
属成分の補給を期待し得ることから簡便であり、また電
極面でのガス発生も少く、従つてとくに大電流を投入し
て厚めつきするような用途で好適である。By the way, in normal electroplating, there are cases where an insoluble electrode is used as an anode, and cases where the metal to be plated is used as a soluble electrode, and in the latter case, maintenance and management of the plating solution is particularly important. It is convenient because it can be expected to constantly replenish the plating metal component from the anode, and there is little gas generation on the electrode surface, so it is particularly suitable for applications where thick plating is performed by applying a large current.
しかるにこの場合アノードがめつきの進行につれて溶出
し、その肉厚減少により通電ギャップは次第に拡大し、
そこでの通電抵抗の増大により電流密度が漸減し、その
結果めつき付着量が漸次に減少するようになる。However, in this case, the anode elutes as plating progresses, and as the thickness decreases, the current carrying gap gradually expands.
The current density gradually decreases due to the increase in current-carrying resistance there, and as a result, the amount of plating deposit gradually decreases.
そこで可溶性電極を用いる上記めつき方式では、該電極
の経時的な消耗に応じる通電ギャップの拡大を、逐次に
修正することが必要である。この通電ギャップの逐次修
正のために従来から、それぞれ弓形をなして電解槽内の
通電用回転ドラムを部扮分的に囲む、消耗電極片の多数
を、通電用回転ドラムの円筒母線に沿う順送り移動可能
に横並べして、この順送り移動を、その1ピッチ毎にそ
の間における該電極片の消耗代だけ、通電用回転ドラム
に近づくような勾配を付した案内.により導き、この案
内また、消耗電極片の群よりなる陽極の全体にわたる給
電にも役立たせるようにされている。Therefore, in the above-mentioned plating method using a soluble electrode, it is necessary to successively correct the expansion of the current conduction gap in response to wear of the electrode over time. In order to successively correct this energization gap, conventionally, a large number of consumable electrode pieces each having an arcuate shape and partially surrounding the energizing rotating drum in the electrolytic cell are sequentially fed along the cylindrical generatrix of the energizing rotating drum. The guides are movably arranged side by side, and the guides are sloped so that the progressive movement approaches the energizing rotating drum by the amount of wear of the electrode piece during each pitch. This guidance also serves to feed the entire anode consisting of a group of consumable electrode pieces.
この案内はしばしば、電極サポートと呼はれる。従つて
通電用回転ドラムの片側で新しい消耗電!極片を、また
他側から使い古しのやせた消耗電極片を、それぞれ着脱
する手順を含めた消耗電極の順送り移動により通電ギャ
ップの修正を伴う組立て電極つまりアノードの逐次更新
が行われる。This guide is often referred to as an electrode support. Therefore, new consumable power is consumed on one side of the energizing rotating drum! By sequentially moving the consumable electrode, including the steps of attaching and detaching the pole piece and the worn out consumable electrode piece from the other side, the assembled electrode, that is, the anode, is successively updated with correction of the current carrying gap.
ここに電極サポートとしてはまずめつき液に侵4されず
かつ過電圧が小さく、そして安価であることなど、この
種の設備に必要な条件を満たすように通常は、方形のか
なり大きい断面(ほぼ450×450Tn!n)に成形
した黒鉛棒より主として成るものとされる。この電極サ
ポートは、電解槽の槽底で正確に位置定めされなければ
、上記通電ギャップを上記アノードの逐次更新の下に正
しく保持することができないので、従来は、槽底に堅固
に取付けられた固定受台に、Vみぞを上向きに形成する
L形鋼を芯材とする支持トラフを介して、第1図A,b
のように保持される。The electrode support is usually made of a fairly large rectangular cross-section (approximately 450 mm x450Tn!n) is mainly formed from a graphite rod. This electrode support must be precisely positioned at the bottom of the electrolytic cell to properly hold the current-carrying gap under the successive updates of the anode, so conventionally this electrode support is rigidly attached to the bottom of the electrolytic cell. Figures 1A and b are attached to the fixed pedestal via a support trough made of L-beam core with an upward V-groove.
It is retained as follows.
図中1は通電用回転ドラム、2はその下半周に沿つて、
電解槽T内を浴浸通板ノ中の金属ストリップであり、3
は通電用回転ドラム1に対しその半径方向に金属ストリ
ップ2との間に通電ギャップGを隔てて向い合う消耗電
極片3″の横並べ群よりなるアノードを示し、アノード
3は、通常図示したように通電用回転ドラム1・の軸心
を挾んで、図に矢印で示した金属ストリップ2の浴浸通
板の前後に対設するように、各消耗電極片3″の背面中
央に隆起形成した突起4により電極サポート5の載置面
6に沿う順送り移動を可能に係止し、この電極サポート
3を支持トラフ”7を介して槽底に設置される固定受台
8によつて堅固に取付けていたのである。しかるにこの
場合は、アノード3の通電ギャップGを設定する電極サ
ポート5が適切に位置定めされているときでも、たとえ
ば金属ストリップ2の板幅が、2″のように広くなつた
とすると、第2図A,bに比較して示すように、とくに
アノード3の両端附近で広幅ストリップ2″に対する通
電ギャップG″G″が、それまでの電解過程で生じたア
ノード3の消耗挙動の下でより狭くなり、ここにエッジ
オーバーコートなどめつき付着量不均斉による外観不良
の原因となる。In the figure, 1 is a rotating drum for energization, 2 is along the lower half of the drum,
A metal strip is passed through the bath immersion plate inside the electrolytic tank T, and 3
1 shows an anode consisting of a horizontally arranged group of consumable electrode pieces 3'' facing a metal strip 2 in the radial direction with respect to the current-carrying rotary drum 1, with a current-carrying gap G between them. A protuberance is formed at the center of the back surface of each consumable electrode piece 3'' so as to sandwich the axis of the energizing rotating drum 1 and to oppose the front and back of the bath immersion plate of the metal strip 2 shown by the arrow in the figure. The protrusion 4 locks the electrode support 5 so that it can be moved sequentially along the mounting surface 6, and the electrode support 3 is firmly attached via the support trough 7 to the fixed pedestal 8 installed on the tank bottom. However, in this case, even when the electrode support 5 that sets the current carrying gap G of the anode 3 is properly positioned, if the plate width of the metal strip 2 is increased, for example by 2'', Then, as shown by comparing FIGS. 2A and 2B, the current conduction gap G"G" relative to the wide strip 2", especially near both ends of the anode 3, is affected by the wear behavior of the anode 3 that occurred during the electrolysis process up to that point. It becomes narrower at the bottom, which causes poor appearance due to uneven coating amount due to edge overcoat.
そこでこの発明は、上記のようなめつき操業条件の変動
などに応じて、適切な調整を行うことができるように、
電極サポート5の支持手段について工夫を凝らしたもの
である。Therefore, the present invention has been developed to enable appropriate adjustments to be made in accordance with the above-mentioned fluctuations in plating operating conditions.
The supporting means for the electrode support 5 is devised.
すなわちこの発明は、電解液を湛えた槽内における金属
ストリップの浴浸通板を司る通電用回転ドラムの槽内浸
漬半周を2等分した各領域に対し、両領域にまたがつて
該ドラムの周面に沿う金属ストリップに面して半径方向
に均整な通電ギャップを隔て向い合わせに通電用回転ド
ラムと同心配置したそれぞれが弓形をなす消耗電極片群
を、通電用回転ドラムの円筒母線に沿う順送り移動可能
に横並べする載置面をもつ一対の電極サポートてそれぞ
れ保持し、該順送り移動により消耗電極片の逐次更新を
行うラジアルセル型電解槽の組立電極支持装置において
、電極サポートの浴中懸垂姿勢を保持する受台に吊手を
設け、この吊手の浴面上に立上りさらに電解槽の槽壁上
縁をこえてから槽外て下向きにのびを吊掛部の下縁を消
耗電極片群の通電回転ドラムに対する同心関係のまま進
退可能な保持に供する並進ガイドを該槽壁にブラケット
で固定したことを特徴とする、ラジアルセル型電解槽に
おける組立て電極支持装置の通電ギャップ調整装置であ
る。In other words, the present invention provides a method for dividing the immersion half circumference of a current-carrying rotary drum into two equal parts in a tank filled with an electrolytic solution, for passing a metal strip through the bath. A group of consumable electrode pieces each having an arcuate shape are arranged concentrically with the energizing rotating drum facing the metal strip along the circumferential surface with a radially uniform energizing gap in between, and are arranged along the cylindrical generatrix of the energizing rotating drum. In an electrode support device for assembling a radial cell type electrolytic cell, a pair of electrode supports each having a horizontally arranged mounting surface that can be moved sequentially is held, and consumable electrode pieces are sequentially renewed by the sequential movement. A hanging hand is provided on the pedestal that maintains the hanging position, and the hanging hand rises above the bath surface, and then extends downward beyond the upper edge of the tank wall of the electrolytic cell, and then attaches the lower edge of the hanging part to the consumable electrode. An energization gap adjustment device for an assembled electrode support device in a radial cell type electrolytic cell, characterized in that a translation guide for holding a group of energized rotating drums in a concentric manner so that they can advance and retreat is fixed to the tank wall with a bracket. be.
第3図にこの発明を具体化したアノード3の電解槽(図
示略)内配置を図解し、9は電極サポート5の支持トラ
フ7を介した、浴中懸垂姿勢を保持する受台で、この受
台9はそのエンドピース10に一対のクレビス11a,
11bを設けて、吊手12の2又脚端とピン12″て連
結し、吊手12は、図にはあられしてない電解槽内の浴
面から立上り、さらに該槽の側壁上縁をこえて下向きに
のびる吊掛部13の下縁14を、該側壁の外面に固定し
た並進ガイド15に沿つて進退可能とする。FIG. 3 illustrates the arrangement of the anode 3 embodying the present invention in an electrolytic cell (not shown), where 9 is a pedestal that maintains a suspended posture in the bath via the support trough 7 of the electrode support 5. The pedestal 9 has a pair of clevises 11a on its end piece 10,
11b is provided and connected to the bifurcated leg end of the hanger 12 with a pin 12'', and the hanger 12 rises from the bath surface in the electrolytic tank (not shown in the figure) and further extends over the upper edge of the side wall of the tank. The lower edge 14 of the hanging portion 13 extending downwardly can move back and forth along a translation guide 15 fixed to the outer surface of the side wall.
図中16はその操作ハンドルである。操作ハンドル16
は第4図A,bに示すように、電解槽Tの側壁Wに溶接
固定したブラケット17に取付けたウォーム歯車箱18
内のウォーム軸の端部に楔止めし、このウォーム軸は該
歯車箱18内のウォーム、ウォームギヤかみ合いにより
作動するねじジヤツキステム19のエンドピース20に
吊掛部13の下縁14を挾みピン2『で連結する一方、
吊掛部13の下縁14には、スラ.イダ21を倒立T字
断面となるように設けて、このスライダ21の摺動を導
く並進ガイド22を、やはり側壁W上のブラケット23
上に設ける。Reference numeral 16 in the figure is its operating handle. Operation handle 16
As shown in FIGS. 4A and 4B, the worm gear box 18 is attached to the bracket 17 welded to the side wall W of the electrolytic cell T.
The worm shaft is wedged to the end of the worm shaft in the gear box 18, and the lower edge 14 of the hanging part 13 is held between the end piece 20 of the screw jack stem 19, which is operated by the engagement of the worm and the worm gear in the gear box 18. ``While connecting with
The lower edge 14 of the hanging portion 13 has a slot. The slider 21 is provided to have an inverted T-shaped cross section, and the translation guide 22 that guides the sliding movement of the slider 21 is connected to a bracket 23 on the side wall W.
Place it on top.
なお図中24は摺動代の指示目盛、25は指針である。
スライダ21、従つて吊掛部13の移動方向は、第4図
bに示すように、電極サポート5の中心を含む通電用回
転ドラム1の半径面と平行に定めることにより、アノー
ド3の金属ストリップ2に面する通電ギャップが上下不
均整を生じることなしに、その拡大と縮小の調節が容易
に槽外操作で行えるわけである。In the figure, 24 is a sliding distance indication scale, and 25 is a pointer.
The moving direction of the slider 21, and thus the hanging part 13, is set parallel to the radial surface of the energizing rotating drum 1 including the center of the electrode support 5, as shown in FIG. 4b, so that the metal strip of the anode 3 The expansion and contraction of the current-carrying gap facing the tank 2 can be easily adjusted by operating outside the tank without causing any vertical asymmetry.
この調節操作系は、電極サポート5の両端でそれぞれ個
別な動作が加えられるので、かような操作により、電極
サポート5を、通電用回転ドラム1の母線に対する勾配
に関して変更調節に供することができるので、種々な金
属ストリップの板幅に容易に適合させ、消耗電極片3″
の有効利用による、アノード原単位の改善も期待できる
。In this adjustment operation system, individual operations are applied at both ends of the electrode support 5, so that by such operation, the electrode support 5 can be subjected to change adjustment with respect to the slope with respect to the generatrix of the rotating drum 1 for energization. , easily adaptable to various metal strip widths, consumable electrode pieces 3″
It is also expected that the anode consumption rate will improve through the effective use of fuel.
上述のようにしてこの発明によれば、組立て電極の金属
ストリップと向い合う通電ギャップを、その板厚の向き
に沿つて槽外から任意に調節して、電解条件の適合を成
就することができ、とくに金属ストリップの板幅の拡大
の際に問題となるエッジオーバーコートの発生傾向を緩
和し、また消耗電極片の廃品化に至る消耗代を適正なら
しめてその原単位を向上するのに有効に役立つ。As described above, according to the present invention, the current-carrying gap facing the metal strip of the assembled electrode can be arbitrarily adjusted from outside the tank along the direction of the plate thickness to achieve matching of the electrolytic conditions. It is particularly effective in alleviating the tendency for edge overcoat to occur, which is a problem when expanding the width of metal strips, and in improving the consumption rate by optimizing the cost of consumable electrodes that lead to their being scrapped. Helpful.
第1図A,bは、従来のラジアルセル型電解槽における
槽内配置を示した側面図と断面図、第2図A,bは処理
中の金属ストリップの幅拡大に伴うエッジオーバーコー
トの発生傾向を示す説明図、第3図はこの発明の具体例
を示す槽内配置の外観図、第4図A,bは調整装置操作
系の側面図と端面図である。
1・・・・・・通電用回転ドラム、2・・・・・・金属
ストリップ、3・・・・・・組立て電極(アノード)、
3″・・・・・弓形消耗電極、5・・・・・・電極サポ
ート、6・・・・・・載置面、7・・・・・・支持サポ
ート、9・・・・・・受台、12・・・・・・吊手、1
3・・・・・・吊掛部、14・・・・・下縁、22・・
・・・・並進ガイド、23・・・・・・ブラケット。Figures 1A and b are side views and cross-sectional views showing the internal arrangement of a conventional radial cell type electrolytic cell, and Figures 2A and b are the occurrence of edge overcoat as the width of the metal strip increases during processing. FIG. 3 is an external view of the arrangement inside the tank showing a specific example of the present invention, and FIGS. 4A and 4B are a side view and an end view of the adjustment device operating system. 1...Rotating drum for current supply, 2...Metal strip, 3...Assembling electrode (anode),
3″... Arcuate consumable electrode, 5... Electrode support, 6... Placement surface, 7... Support support, 9... Receiving Stand, 12... Hanging hand, 1
3...Hanging part, 14...Lower edge, 22...
...Translation guide, 23...Bracket.
Claims (1)
通板を司る通電用回転ドラムの槽内浸漬半周を2等分し
た各領域に対し、両領域にまたがつて該ドラムの周面に
沿う金属ストリップに面して半径方向に均整な通電ギャ
ップを隔て向い合わせに通電用回転ドラムと同心配置し
たそれぞれが弓形をなす消耗電極片群を、通電用回転ド
ラムの円筒母線に沿う順送り移動可能に横並べする載置
面をもつ一対の電極サポートでそれぞれ保持し、該順送
り移動により消耗電極片の逐次更新を行うラジアルセル
型電極槽の組立電極支持装置において、電極サポートの
浴中懸垂姿勢を保持する受台に吊手を設け、この吊手の
浴面上に立上りさらに電解槽の槽壁上縁をこえてから槽
外で下向きにのびる吊掛部の下縁を消耗電極片群の通電
回転ドラムに対する同心関係のまま進退可能な保持に供
する並進ガイドを該槽壁にブラケットで固定したことを
特徴とする、ラジアルセル型電解槽における組立電極支
持装置の通電ギャップ調整装置。1. For each region that divides the immersion half-circumference of the energizing rotating drum, which controls the bath immersion plate of the metal strip in the tank filled with electrolyte into two, along the circumferential surface of the drum across both regions. A group of consumable electrode pieces, each arcuate in shape, are arranged concentrically with the energizing rotating drum, facing the metal strip across a radially balanced energizing gap, and can be moved sequentially along the cylindrical generatrix of the energizing rotating drum. In an electrode support device for assembling a radial cell type electrode bath, which is held by a pair of electrode supports with side-by-side mounting surfaces and sequentially updates consumable electrode pieces by sequential feeding, the electrode support is maintained in a suspended position in the bath. A hanging hand is provided on the pedestal, and the lower edge of the hanging part that rises above the bath surface and extends downward outside the electrolytic cell after passing over the upper edge of the tank wall of the electrolytic cell is connected to the energizing rotation of the group of consumable electrode pieces. 1. An energization gap adjustment device for an assembled electrode support device in a radial cell type electrolytic cell, characterized in that a translation guide for holding the drum so that it can move forward and backward in a concentric relationship with the drum is fixed to the tank wall with a bracket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3220782A JPS6058317B2 (en) | 1982-03-03 | 1982-03-03 | Current flow gap adjustment device for assembly electrode support device of radial cell type electrolyzer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3220782A JPS6058317B2 (en) | 1982-03-03 | 1982-03-03 | Current flow gap adjustment device for assembly electrode support device of radial cell type electrolyzer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58151498A JPS58151498A (en) | 1983-09-08 |
| JPS6058317B2 true JPS6058317B2 (en) | 1985-12-19 |
Family
ID=12352456
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3220782A Expired JPS6058317B2 (en) | 1982-03-03 | 1982-03-03 | Current flow gap adjustment device for assembly electrode support device of radial cell type electrolyzer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6058317B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100793587B1 (en) * | 2001-12-27 | 2008-01-14 | 주식회사 포스코 | Carbon bridge changer for electroplating |
-
1982
- 1982-03-03 JP JP3220782A patent/JPS6058317B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58151498A (en) | 1983-09-08 |
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