JPH0768628B2 - Electrode plate treatment method in electrolytic smelting - Google Patents

Electrode plate treatment method in electrolytic smelting

Info

Publication number
JPH0768628B2
JPH0768628B2 JP62096291A JP9629187A JPH0768628B2 JP H0768628 B2 JPH0768628 B2 JP H0768628B2 JP 62096291 A JP62096291 A JP 62096291A JP 9629187 A JP9629187 A JP 9629187A JP H0768628 B2 JPH0768628 B2 JP H0768628B2
Authority
JP
Japan
Prior art keywords
electrode plate
plate
plates
electrode
anode
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
JP62096291A
Other languages
Japanese (ja)
Other versions
JPS63262494A (en
Inventor
皓一 金子
清尊 安部
武夫 木村
満 大小田
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
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 Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP62096291A priority Critical patent/JPH0768628B2/en
Priority to EP88105556A priority patent/EP0286093B1/en
Priority to DE88105556T priority patent/DE3881933T2/en
Priority to AU14430/88A priority patent/AU595996B2/en
Priority to US07/179,543 priority patent/US5002642A/en
Priority to CA000563645A priority patent/CA1329382C/en
Priority to KR1019880004054A priority patent/KR940002259B1/en
Priority to FI881677A priority patent/FI87659C/en
Publication of JPS63262494A publication Critical patent/JPS63262494A/en
Priority to AU49039/90A priority patent/AU625401B2/en
Publication of JPH0768628B2 publication Critical patent/JPH0768628B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は陰陽両極板を同時に電解槽から引き上げ、各種
極板処理を行う電解製錬における極板処理方法に関す
る。
TECHNICAL FIELD The present invention relates to an electrode plate treatment method in electrolytic smelting in which both positive and negative electrode plates are pulled out of an electrolytic cell at the same time to perform various electrode plate treatments.

[従来技術と問題点] 電解製錬の代表的な一例である亜鉛電解においては、電
解槽に装入されている陰陽両極板は以下の処理例に示さ
れるように従来、互いに分離して処理されている。
[Prior Art and Problems] In zinc electrolysis, which is a typical example of electrolytic smelting, the Yin-Yo bipolar plates charged in the electrolytic cell are conventionally separated from each other as shown in the following processing example. Has been done.

陰極板の処理工程例 (a)陰極板を電解槽から吊上げる→(b)陰極板の洗
浄→(c)電着金属の剥離→(d)陰極板を電解槽へ装
入→(e)電解継続 陽極板の処理工程例 (a)電解槽の通電停止→(b)陰極板の取出し→
(c)電解液の抜出し→(d)陽極板の取出し→(e)
必要に応じ電解槽の掃除→(f)陽極板からクラストを
除去→(g)陽極板の洗浄、プレス等→(h)陰陽両極
板の電解槽への装入→(i)電解液の供給→(j)電解
再開 以上のように、従来、陰極板は電着金属を剥離する都度
電解槽から引き上げられ、剥離前後に種々の極板処理が
施された後に再び電解槽に装入されるが、陽極板は数回
の電解サイクルが繰り返された後に、電解槽から引き上
げられ、極板表面に付着するクラストの除去等の各種整
備作業が施される。従来、陰陽両極板を分離して処理し
ている理由は、陰極板に析出する電着金属の剥離が1日
〜4日毎に行われるのに対して陽極板のクラスト除去は
20日〜40日毎に行えば足りると考えられているからであ
る。クラスト除去のため陽極板の整備サイクルを短くす
れば、作業回数の増加による負担を招く。特に、従来、
陰陽両極板は夫々一枚づつ電解槽に吊り下げられている
のでこれら両極板を夫々引き上げて同時に両極板の処理
を施すのが煩雑であり、作業負担が大きい。其処でクラ
スト除去の作業負担とクラストの除去による消費電力の
軽減効果との兼ね合いから、従来、陽極板のクラスト除
去作業は20日〜40日のサイクルで行っている。然し乍
ら、陽極板のクラストは電解抵抗となり、クラストが厚
くなるほど電解効率は低下するので、電解効率を高める
観点からはクラストは出来るだけ早期に除去することが
望ましい。また、クラストの付着量が少ないほど陽極板
の整備作業が容易であるので、この点でも陽極板の整備
サイクルが短期間であることが望ましい。
Example of cathode plate treatment process (a) Lifting the cathode plate from the electrolytic cell → (b) Cleaning the cathode plate → (c) Removing the electrodeposited metal → (d) Inserting the cathode plate into the electrolytic cell → (e) Continuation of electrolysis Example of anode plate treatment process (a) Stop energization of electrolytic cell → (b) Take out cathode plate →
(C) Extraction of electrolyte solution → (d) Removal of anode plate → (e)
If necessary, clean the electrolytic cell → (f) remove the crust from the anode plate → (g) clean the anode plate, press, etc. → (h) load the positive and negative electrode plates into the electrolytic cell → (i) supply the electrolytic solution → (j) Resuming electrolysis As described above, conventionally, the cathode plate is pulled up from the electrolytic bath every time the electrodeposited metal is peeled off, various electrode plate treatments are carried out before and after the peeling, and then the electrolytic plate is charged again. However, after the electrolysis cycle is repeated several times, the anode plate is pulled out of the electrolytic cell and various maintenance work such as removal of crust adhering to the surface of the electrode plate is performed. Conventionally, the reason why the positive and negative electrode plates are separated and treated is that the electrodeposited metal deposited on the cathode plate is peeled off every 1 to 4 days, but the crust removal on the anode plate is
It is believed that it is sufficient to do it every 20 to 40 days. If the maintenance cycle of the anode plate is shortened to remove the crust, the number of operations increases, which causes a burden. Especially,
Since each of the Yin-Yo bipolar plates is suspended in the electrolytic cell one by one, it is troublesome to pull up each of the bipolar plates and treat the bipolar plates at the same time, resulting in a heavy work load. Therefore, in order to balance the work load of crust removal and the power consumption reduction effect of crust removal, the crust removal work of the anode plate is conventionally performed in a cycle of 20 to 40 days. However, the crust of the anode plate becomes an electrolytic resistance, and the thicker the crust, the lower the electrolytic efficiency. Therefore, from the viewpoint of increasing the electrolytic efficiency, it is desirable to remove the crust as early as possible. Further, the smaller the amount of crust adhered, the easier the maintenance work of the anode plate is. Therefore, in this respect as well, it is desirable that the maintenance cycle of the anode plate is short.

また、従来、陽極板の整備は特定の電解槽の陰陽両極板
全部を取り出すため、通電を停止して行っており、極板
処理作業の間この電解槽での電解が中断する問題があ
る。
Further, conventionally, the maintenance of the anode plate is performed by stopping the energization in order to take out all the positive and negative electrode plates of a specific electrolytic cell, and there is a problem that the electrolysis in this electrolytic cell is interrupted during the electrode plate processing operation.

[問題解決の手段] 本発明は、クレーンなどの吊り上げ移送手段を用いて陰
陽両極板を同時に吊り上げ、両極板を該移送手段に保持
したまま一連の極板処理を連続して行うことにより、陰
極板の電着金属の剥離作業に付随して陽極板の整備作業
を行い、該整備作業の負担をあまり増加せずに陽極板の
クラストを除去し、これにより従来の問題を解決して電
解効率の向上を図った。
[Means for Solving Problems] The present invention uses a hoisting and transferring means such as a crane to simultaneously hoist the positive and negative electrode plates, and continuously carries out a series of electrode plate treatments while holding the both electrode plates on the hoisting and transferring means. Anode plate maintenance work is carried out in association with the work of stripping the electrodeposited metal on the plate, and the crust of the anode plate is removed without significantly increasing the burden of the maintenance work, thereby solving the conventional problems and improving the electrolysis efficiency. To improve.

[発明の構成] 本発明によれば以下の構成からなる極板処理方法が提供
される。
[Structure of the Invention] According to the present invention, there is provided an electrode plate processing method having the following structure.

(1)(イ)複数の陽極板と陰極板を絶縁性の型枠を介
して交互に一定間隔ごとに一体に連結した極板ユニット
を形成し、該極板ユニットを電解槽に装入して電解を行
った後に、(ロ)多数の摺動自在な陽極ハンガーと陰極
ハンガーを有し、これら陽極ハンガーと陰極ハンガーが
相互に絶縁され、各ハンガーには極板を吊下げるフック
が装着されており、該ハンガーに極板を吊下げた状態で
搬送する移送クレーンを用い、(ハ)極板ユニットの各
陽極板および各陰極板を移送クレーンの各ハンガーに吊
下げて極板ユニットを電解槽から引上げ、(ニ)該ハン
ガーの移動により、各極板を吊下げた状態で互いに引き
離して極板間隔を広げ、(ホ)極板間隔を広げて吊下げ
た状態で、電着金属の剥離、極板洗浄および極板表面の
研磨を含む極板処理を行い、(ヘ)極板処理後、極板を
吊り下げているハンガーを接近させて交互に配列されて
いる陽極板と陰極板との間隔を狭め、型枠を介して一定
間隔に一体化して再び極板ユニットを形成して電解工程
に送ることを特徴とする電解製錬における極板処理方
法。
(1) (a) A plurality of positive electrode plates and negative electrode plates are alternately and integrally connected to each other through an insulating mold to form an electrode plate unit, and the electrode plate units are loaded into an electrolytic cell. (B) Having a large number of slidable anode hangers and cathode hangers, the anode hangers and cathode hangers are insulated from each other, and each hanger is equipped with a hook for hanging the electrode plate. Using a transfer crane that conveys the electrode plate suspended in the hanger, (c) each anode plate and each cathode plate of the electrode plate unit are hung on each hanger of the transfer crane to electrolyze the electrode plate unit. (D) By moving the hanger, the electrode plates are hung from each other to be separated from each other to widen the electrode plate spacing, and (e) The electrode plate is hung with the electrode plate spacing widened to suspend the electrodeposited metal. Electrode plate treatment including peeling, electrode plate cleaning and electrode plate polishing (F) After the electrode plate treatment, the hangers suspending the electrode plates are brought close to each other to narrow the gap between the anode plate and the cathode plate that are alternately arranged, and they are integrated at a constant interval through the formwork. A method of processing an electrode plate in electrolytic smelting, which comprises forming an electrode plate unit again and sending it to an electrolytic process.

(2)複数の陽極板と陰極板を同時にハンガーに吊下
げ、通電中の電解槽から極板ユニットを引上げて極板処
理工程に搬送する上記(1)の極板処理方法。
(2) The electrode plate treatment method according to the above (1), in which a plurality of anode plates and cathode plates are simultaneously hung on a hanger, and the electrode plate unit is pulled up from the energized electrolytic bath and conveyed to the electrode plate treatment step.

(3)多数の極板をハンガーに吊下げた状態で各極板処
理手段の間を通過させる間に吊下げた多数の極板の処理
を同時に行う上記(1)の極板処理方法。
(3) The electrode plate processing method according to (1), in which a large number of electrode plates are simultaneously suspended while being passed between the electrode plate processing means while the electrode plates are suspended on a hanger.

本発明に係る極板処理工程の一例を第1図に示す。第2
図に各処理工程の配置例を示す。
An example of the electrode plate processing step according to the present invention is shown in FIG. Second
The figure shows an example of the layout of each processing step.

図示するように本発明の方法においては、陽極板と陰極
板とが同時に電解槽から引き上げられる。陰陽両極板を
吊上げて移送する手段としてはクレーン等を用いること
が出来る。電気的に絶縁されているクレーンを用いるこ
とにより通電状態の電解槽から陰極板と陽極板とを同時
に吊上げることが出来る。陰陽両極板は電解槽中で、通
常、30〜35mm程度の間隔に保持されており、又、或る種
の型枠を用いることにより15mm程度に近接して配設され
る。上記極板相互の間隔は、陰陽両極板を同時にクーレ
ンから吊り下げて種々の極板処理作業を行なうには狭過
ぎる。そこで、上記クレーンは吊り下げた極板相互の間
隔を拡大及び縮小する機能を有することが望まれる。こ
のようなクレーンとして第3図に示すクレーンを用いる
と良い。
As shown in the figure, in the method of the present invention, the anode plate and the cathode plate are simultaneously pulled up from the electrolytic cell. A crane or the like can be used as a means for lifting and transferring the Yin Yang bipolar plates. By using an electrically insulated crane, the cathode plate and the anode plate can be lifted at the same time from the energized electrolytic cell. The yin and yang bipolar plates are usually held at an interval of about 30 to 35 mm in the electrolytic cell, and they are arranged close to each other by about 15 mm by using a certain form. The distance between the plates is too narrow to perform various plate processing operations by simultaneously suspending the positive and negative plates from the coolen. Therefore, it is desired that the crane has a function of expanding and contracting the interval between the suspended electrode plates. The crane shown in FIG. 3 may be used as such a crane.

図示するようにクレーン10は、電解槽に沿って走行自在
に配設された本体フレーム11と;該本体フレームの走行
機構12と;該本体フレームに装着され、電解槽の上方に
位置する昇降自在なハンガー支持台13と;該ハンガー支
持台に装着された複数の移動自在なハンガー14と;該ハ
ンガーを移動して互いに接近離反させるハンガー移動機
構15と;該ハンガーから吊下げられ極板の耳部に係合す
る傾動自在なフック16と;該フックを傾動して極板耳部
に係合離脱させるフック傾動機構とを有している。上記
ハンガーと上記ハンガー支持台との間に絶縁材が介設さ
れている。また、上記支持台に装着された複数のハンガ
ーを移動して各ハンガーの間隔を拡大、縮小する手段が
設けられている。即ち、各ハンガーは連結リンクを介し
て相互に連結され、他方、上記ハンガー支持台には各ハ
ンガーを互いに逆向きに移動する2連のチェーンが配設
されており、該チェーンおよび上記連結リンクを介によ
り各ハンガーが移動して接近乃至離反し、相互の間隔が
調節される。
As shown in the figure, the crane 10 includes a main body frame 11 arranged so as to be freely movable along the electrolytic cell; a traveling mechanism 12 for the main body frame; and a movable body which is mounted on the main body frame and is located above the electrolytic cell. Hanger support 13; a plurality of movable hangers 14 mounted on the hanger support; a hanger moving mechanism 15 for moving the hangers to move them away from each other; an ear of an electrode plate suspended from the hangers It has a tiltable hook 16 that engages with the portion; and a hook tilting mechanism that tilts the hook to engage with and disengage from the electrode plate ear. An insulating material is provided between the hanger and the hanger support. Further, there is provided means for moving a plurality of hangers mounted on the support base to expand or reduce the interval between the hangers. That is, the hangers are connected to each other via connecting links, while the hanger support is provided with two chains that move the hangers in opposite directions. The hangers are moved by the interposition to move toward or away from each other, and the mutual distance is adjusted.

さらに、上記クレーンは、相互の間隔が狭い極板をも同
時に吊下げることができるように、2種のハンガーを備
える。すなわち、カソード板を吊下げる陰極ハンガーと
アノード板を吊下げる陽極ハンガーを有し、この陽極ハ
ンガーと陰極ハンガーとの間は上記絶縁材によって相互
に絶縁されている。さらに陰極ハンガーは、その両側端
に脚部が形成され、該脚部を介してハンガー支持台上の
ガイドレールに載置されており、該陰極ハンガー脚部の
間に陽極ハンガーが入り込めるように該陰極ハンガーの
脚部は陽極ハンガーよりも高く形成されている。
Further, the crane is provided with two types of hangers so that the polar plates having a small mutual interval can be simultaneously hung. That is, it has a cathode hanger for suspending the cathode plate and an anode hanger for suspending the anode plate, and the anode hanger and the cathode hanger are insulated from each other by the insulating material. Further, the cathode hanger is formed with legs at both ends thereof, and is mounted on the guide rails on the hanger support through the legs so that the anode hanger can be inserted between the legs of the cathode hanger. The legs of the cathode hanger are formed higher than the legs of the anode hanger.

上記電解槽からクレーン10によって引上げられたアノー
ド板(陽極板)1と電着カソード板(陰極板)2はクレ
ーン10により極板間隔を拡げてアノード板整備工程30に
移送される。尚、一例として電解槽内の極板間隔が15〜
30mmであるものが移送中に150〜250mmの間隔に拡げられ
る。
The anode plate (anode plate) 1 and the electrodeposited cathode plate (cathode plate) 2 pulled up from the electrolytic cell by the crane 10 are transferred to the anode plate servicing step 30 by the crane 10 while expanding the electrode plate spacing. As an example, the electrode plate spacing in the electrolytic cell is 15 ~
What is 30mm is spread during the transfer at intervals of 150-250mm.

アノード整備工程30に移送された極板は、該工程を通過
する間にアノード板表面のアノードクラストが除去され
る。該アノード整備工程30に設けられたアノード整備機
31の一例を第4図、第5図に示す。図示するアノード整
備機31はクレーン10から吊下げられた複数の極板1,2が
立設された複数の配管32の間を通過し、クレーン10の水
平移動が妨げられないように構成されている。各配管32
の側面にはアノード板1の表面に向って開口する多数の
ノズル33が設けられている。複数枚の極板1,2がクレー
ン10に吊下げられた状態で並列に各配管32の間に進入し
てくると、位置センサー等によりこの進入が検出され、
アノード板1の両側からノズル33を通じて高圧水がアノ
ード板表面に向って噴射される。アノード板1が配管32
を通過する間、高圧水の噴射が継続され、この水圧によ
りアノード板表面に付着したアノードクラストが除去さ
れる。同時にアノード板側端に装着されている型枠70が
洗浄される。アノード板1が配管32を通過すると、位置
センサー等によりこの通過が検出され、高圧水の噴射が
停止される。以上のように該アノード整備機31では、ア
ノード板1およびカソード板2がクレーン10に吊下げら
れた状態のまま、次のカソード洗浄工程40に向って移送
される間に、複数枚のアノード板1が同時に処理され
る。アノード整備機は上記型式に限らず用いることがで
きる。尚、アノード板2に型枠70が装着されていれば、
アノード板2は湾曲し難いので、従来行われている板面
の湾曲補修作業を省略できる。
The anode plate transferred to the anode maintenance process 30 has the anode crust on the surface of the anode plate removed while passing through the process. Anode maintenance machine provided in the anode maintenance process 30
An example of 31 is shown in FIG. 4 and FIG. The illustrated anode maintenance machine 31 is configured so as to pass between a plurality of pipes 32 in which a plurality of electrode plates 1 and 2 suspended from a crane 10 are erected and to prevent the horizontal movement of the crane 10 from being hindered. There is. Each pipe 32
A large number of nozzles 33 that open toward the surface of the anode plate 1 are provided on the side surface of the. When a plurality of electrode plates 1 and 2 come in parallel between the pipes 32 in a state of being suspended by the crane 10, this entry is detected by a position sensor or the like,
High-pressure water is sprayed from both sides of the anode plate 1 through the nozzles 33 toward the surface of the anode plate. Anode plate 1 is pipe 32
High-pressure water is continued to be jetted while passing through, and the water pressure removes the anode crust adhering to the surface of the anode plate. At the same time, the mold 70 attached to the end on the anode plate side is washed. When the anode plate 1 passes through the pipe 32, this passage is detected by a position sensor or the like, and the injection of high-pressure water is stopped. As described above, in the anode maintenance machine 31, while the anode plate 1 and the cathode plate 2 are suspended from the crane 10, the plurality of anode plates are transferred while being transferred toward the next cathode cleaning step 40. 1s are processed at the same time. The anode maintenance machine is not limited to the above model and can be used. If the mold 70 is attached to the anode plate 2,
Since the anode plate 2 is unlikely to bend, it is possible to omit the conventional work for bending the plate surface.

次にカソード板洗浄工程40に移送された極板は、該工程
を通過する間にカソード板表面が洗浄される。カソード
洗浄機としてはアノード整備機31と同構造のものを用い
ることができる。尚、カソード板洗浄工程40においては
温水を用いると洗浄効果がよい。
Next, the surface of the electrode plate transferred to the cathode plate cleaning step 40 is cleaned while passing through the step. The cathode cleaning machine having the same structure as the anode maintenance machine 31 can be used. In the cathode plate cleaning step 40, warm water is used for good cleaning effect.

尚、アノード板整備とカソード板洗浄とを同時に行って
もよい。上記アノード整備機31の配管32に、夫々アノー
ド板表面とカソード板表面とに向うノズルを設けること
により、アノード板整備とカソード板洗浄とが同時に行
われる。
The anode plate maintenance and the cathode plate cleaning may be performed at the same time. By providing the nozzles facing the surface of the anode plate and the surface of the cathode plate in the pipe 32 of the anode maintenance machine 31, the maintenance of the anode plate and the cleaning of the cathode plate are simultaneously performed.

第4図、第5図に示すアノード整備機31およびカソード
洗浄機を用いることにより、複数枚のアノード板および
カソード板はクレーン10に吊下げられて剥離工程60に向
って水平に移送される間に、アノード板の整備とカソー
ドの洗浄とが行われる。
While the anode maintenance machine 31 and the cathode cleaning machine shown in FIGS. 4 and 5 are used, a plurality of anode plates and cathode plates are hung by the crane 10 and horizontally transferred toward the peeling process 60. First, the anode plate is serviced and the cathode is cleaned.

剥離工程60において、極間距離が拡げられた状態で電着
カソード板2とアノード板1を保持したまま、これら極
板はカソード剥離機にセットされる。該剥離機は第2図
に示すように複数枚の電着カソード板を一度に剥離でき
る型式のものが使用される。アノード板1と電着カソー
ド板2が同時に剥離機61にセットされる。クレーン10に
よって拡げられた電着カソード板相互の間隙は剥離機61
に具備された剥離用ナイフ62a,62bの間隙と同一に設定
され、これら極板1,2をクレーン10に保持した状態のま
ま電着亜鉛が剥離される。
In the peeling step 60, the electrode plates are set in the cathode peeling machine while holding the electrodeposited cathode plate 2 and the anode plate 1 with the distance between the electrodes being expanded. As shown in FIG. 2, the stripping machine is of a type capable of stripping a plurality of electrodeposited cathode plates at once. The anode plate 1 and the electrodeposited cathode plate 2 are simultaneously set in the peeling machine 61. The gap between the electrodeposited cathode plates expanded by the crane 10 is the peeling machine 61.
The gap between the stripping knives 62a and 62b provided in the above is set to be the same, and the electrodeposited zinc is stripped while the electrode plates 1 and 2 are held in the crane 10.

このように剥離操作はハンガーから両方の極板を取り外
すことなく実施されるが、電着カソード板と隣接するア
ノード板との距離を150〜250m/mに保持すればアノード
板が剥離機内に存在しても通常の剥離機でも剥離操作に
支障はない。
In this way, the stripping operation is performed without removing both plates from the hanger, but if the distance between the electrodeposited cathode plate and the adjacent anode plate is maintained at 150 to 250 m / m, the anode plate will be present in the stripper. Even with a normal peeling machine, however, the peeling operation will not be hindered.

電着亜鉛がカソード板2から剥離された後、極板1,2は
カソード研磨工程50に移送される。電着亜鉛を剥離した
後のカソード板の研磨もクレーン10にアノード板1とカ
ソード板2を保持したまま実施される。この工程におい
てもカソード板と隣接するアノード板の距離が150〜250
m/mであれば、カソード板研磨の妨げとならない。
After the electrodeposited zinc is separated from the cathode plate 2, the electrode plates 1 and 2 are transferred to the cathode polishing process 50. Polishing of the cathode plate after stripping the electrodeposited zinc is also carried out while the crane 10 holds the anode plate 1 and the cathode plate 2. Even in this process, the distance between the cathode plate and the adjacent anode plate is 150 to 250.
If it is m / m, it does not hinder the polishing of the cathode plate.

カソード研磨機51の一例を第6図、第7図に示す。該研
磨機51はクレーン10から吊下げられた複数の極板1,2が
立設された複数の研磨ブラシの間を通過し、このときカ
ソード板2が一対の研磨ブラシ52a,52bに圧接して通過
するように構成されている。研磨ブラシ52a,52bは水平
回転され、カソード板2が通過する間に極板表面を、回
転研磨する。研磨ブラシ52a,52bの回転方向および回転
速度はクレーン10の移送方向及び速度に応じて適宜調整
される。尚、アノード板2の側端に型枠70を設けカソー
ド板2と密着して電解槽に配設すれば、カソード板2の
側端には従来のような絶縁材を取付ける必要がなく、従
って、研磨ブラシ52a,52bの間隙も固定できるので研磨
機の機構が簡略化できる。
An example of the cathode polishing machine 51 is shown in FIGS. 6 and 7. The polishing machine 51 passes between a plurality of polishing brushes on which a plurality of electrode plates 1 and 2 suspended from a crane 10 are erected. At this time, the cathode plate 2 is pressed against a pair of polishing brushes 52a and 52b. Are configured to pass through. The polishing brushes 52a and 52b are horizontally rotated to rotationally polish the surface of the electrode plate while the cathode plate 2 passes. The rotation direction and rotation speed of the polishing brushes 52a and 52b are appropriately adjusted according to the transfer direction and speed of the crane 10. If the mold 70 is provided at the side end of the anode plate 2 and is closely attached to the cathode plate 2 and disposed in the electrolytic cell, it is not necessary to attach an insulating material to the side end of the cathode plate 2 as in the conventional case. Since the gap between the polishing brushes 52a and 52b can be fixed, the mechanism of the polishing machine can be simplified.

上記カソード研磨機51を通過した極板1,2は、クレーン1
0が電解槽に向って移動する間に該極板を吊下げている
アノードハンガーおよびカソードハンガーが互いに接近
するように移動され、極板間隙が縮小され、型枠を介在
してアノード板とカソード板とが交互に密接した状態に
配列される。このように一体化された極板の配列が電解
槽に降下され、該極板を取出した箇所に再び装入され
る。
The plates 1 and 2 that have passed through the cathode polishing machine 51 are the crane 1
While 0 moves toward the electrolytic cell, the anode hanger and the cathode hanger that suspend the electrode plate are moved so as to approach each other, the electrode plate gap is reduced, and the anode plate and the cathode plate are intervened with the formwork interposed. The plates and the plates are alternately arranged in close contact with each other. The array of electrode plates integrated in this way is lowered into the electrolytic cell, and the electrode plates are reloaded at the location where they are taken out.

上記本発明の処理方法においては、1サイクルの処理工
程において取扱の極板の枚数は任意であるが、作業能率
を高める観点から、その一例として1つの電解槽につい
て1/2槽分の極板を処理し、上記処理工程を2サイクル
繰返すことにより1槽分の極板処理を終了させればよ
い。尚、1/2槽分の極板が引下げられた後、再び装入さ
れる間に、該電解槽に生じた空間を利用して電解槽を掃
除することができる。このとき電解槽底部にアノードク
ラストの落下物が堆積している場合には、槽底のクラス
トを吸引する手段を用いることにより電解槽への通電を
停止せずに電解槽の底部を掃除することができる。
In the treatment method of the present invention, the number of electrodes to be handled in one treatment step is arbitrary, but from the viewpoint of improving work efficiency, as one example, one electrolytic cell is equivalent to 1/2 electrode plate. And the above process is repeated for two cycles to complete the electrode plate treatment for one tank. It should be noted that the electrolytic cell can be cleaned by utilizing the space created in the electrolytic cell while the electrode plate for 1/2 cell is pulled down and then charged again. At this time, if fallen items of the anode crust are accumulated on the bottom of the electrolytic cell, the bottom of the electrolytic cell should be cleaned without stopping energization to the electrolytic cell by using a means for sucking the crust on the bottom of the electrolytic cell. You can

本発明の処理方法における一連の処理操作は、各工程に
配設されている処理装置およびクレーンに夫々内蔵した
自動制御機構により自動的に行うようにするとよい。該
自動制御機構としては位置センサー、制御回路部等を具
えた通常のものを用いることができる。
A series of processing operations in the processing method of the present invention may be automatically performed by an automatic control mechanism incorporated in each of the processing device and the crane arranged in each step. As the automatic control mechanism, a normal one having a position sensor, a control circuit unit, etc. can be used.

また、上記処理工程において、極板の洗浄工程及びクラ
スト除去工程は毎回行なわず、処理工程を数回行なう際
に1回行なうようにしても良い。
Further, in the above-described processing step, the electrode plate cleaning step and the crust removing step may not be performed each time, but may be performed once when the processing step is performed several times.

更に、上記処理工程において、剥離工程から極板の研磨
工程に至る間に損傷した極板及び型枠が検出され、他の
極板及び型枠に取替えられる。
Further, in the above-mentioned processing step, the electrode plate and the mold damaged during the peeling process to the electrode plate polishing process are detected and replaced with another electrode plate and the frame.

以上、第1図に示す処理方法について、第2図の配置図
を参照して説明したが、本発明の処理方法は上記工程を
経由する方法に限らず、また第2図の配置例によるもの
に限らない。更に、極板の洗浄装置乃至整備装置は図示
する構成の装置に限らない。
The processing method shown in FIG. 1 has been described above with reference to the layout diagram of FIG. 2. However, the processing method of the present invention is not limited to the method of passing through the above steps, and is based on the layout example of FIG. Not limited to Further, the electrode plate cleaning device and the maintenance device are not limited to the devices having the illustrated configurations.

[発明の効果] 本発明の処理方法では、通電状態の電解槽からアノード
板と電着カソード板を同時に機械的に引上げるため、従
来のようなこれらの極板を別々に引上げる方法と異な
り、作業量が増加せず、むしろこれらの極板をクレーン
に吊下げた状態で連続的に各工程の処理を行うので従来
の方法に比べ、一連の作業をより迅速に実施することが
できる。
[Effects of the Invention] In the treatment method of the present invention, the anode plate and the electrodeposited cathode plate are mechanically pulled simultaneously from the electrolyzer in the energized state, which is different from the conventional method of pulling these electrode plates separately. However, the work amount does not increase, and rather, the process of each step is continuously performed in a state where these electrode plates are suspended in a crane, so that a series of work can be performed more quickly than in the conventional method.

因に、図示する型式のアノード整備機およびカソード洗
浄機を用いることによりクレーンの水平移動中にこれら
の処理を行うことができるので一層処理時間が短縮され
る。
By using the illustrated type of anode maintenance machine and cathode cleaning machine, these treatments can be performed during horizontal movement of the crane, which further shortens the treatment time.

従来の方法では、アノード板の整備や、電着カソード板
からの電着亜鉛の剥離、カソード板の研磨等の各処理作
業を実施するには何れもストックコンベアが必要であっ
た。ストックコンベアを設置するには電解工場に広い建
屋面積が必要となる。本発明においては、ストックコン
ベアを全く用いる必要がなく、比較的小さい建屋面積で
極板の一連の処理を効果的に行うことができる。
In the conventional method, a stock conveyor is required to carry out various processing operations such as maintenance of the anode plate, peeling of electrodeposited zinc from the electrodeposited cathode plate, and polishing of the cathode plate. To install a stock conveyor, a large building area is required in the electrolytic plant. In the present invention, it is not necessary to use a stock conveyor at all, and a series of treatments of the electrode plate can be effectively performed with a relatively small building area.

また、多数枚の極板をクレーンに保持したまま1度に処
理できるので処理能力が大きく、かつ極板を保持したク
レーンから各工程への極板の移載が不要であり、ストッ
クコンベアからアノード整機、剥離機、研磨機等への移
載及びこれらの機器からストックコンベアへの移載及び
ストックコンベアからクレーンへの移載設備が全て不要
であるので処理工程を簡単化できる。
In addition, since a large number of plates can be processed at one time while being held in the crane, the processing capacity is large, and there is no need to transfer the plates from the crane holding the plates to each process, and the stock conveyor to the anode It is possible to simplify the treatment process because transfer equipment such as a leveling machine, a peeling machine, and a polishing machine, transfer equipment from these devices to a stock conveyor, and transfer equipment from a stock conveyor to a crane are all unnecessary.

本発明の処理方法は、極板の移送中に極板相互の間隙を
拡大縮小することにより電解槽中の極板間隔が狭い極板
についても実施することが出来、従来の電解槽の極板、
或いは、極板型枠を用いて極板間隔を更に狭めた電解槽
の極板についても本発明の処理方法を適宜することがで
きる。従って極板の間に型枠を介在して複数の極板を一
体化した極板配列に対しても効果的に一連の処理を実施
できる。例えばアノード板にその外周を囲む型枠を取付
け、この型枠を介在してアノード板とカソード板を交互
に密着して配列し、カセット状に一体化したものは、従
来の電解槽に比べ、極板間隔が小さく、電解槽を小型化
出来る利点が在る。また電解槽に多数の極板を装入する
のが容易である等の利点を有する。本発明の方法は陰陽
両極板を同時に吊上げるので、かかる一体型の極板に対
して本発明の処理方法を実施すれば、極板を個々に取り
外す必要が無く、その極板処理を極めて効率的に行なう
ことが出来る。
The treatment method of the present invention can be carried out on a plate having a narrow electrode plate spacing in an electrolytic cell by enlarging or reducing the gap between the electrode plates during transfer of the electrode plate. ,
Alternatively, the treatment method of the present invention can be appropriately applied to the electrode plate of the electrolytic cell in which the electrode plate space is further narrowed by using the electrode plate frame. Therefore, a series of treatments can be effectively carried out even on an electrode plate array in which a plurality of electrode plates are integrated with a frame interposed between the electrode plates. For example, a mold surrounding the outer periphery of the anode plate is attached, the anode plate and the cathode plate are arranged in close contact with each other by interposing this mold, and the one integrated in a cassette shape is There is an advantage that the electrode plate interval is small and the electrolytic cell can be downsized. Further, there are advantages that it is easy to load a large number of electrode plates into the electrolytic cell. Since the method of the present invention simultaneously lifts both the positive and negative electrode plates, if the treatment method of the present invention is carried out on such an integral type electrode plate, it is not necessary to remove the electrode plates individually, and the electrode plate processing is extremely efficient. Can be done on a regular basis.

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

第1図は本発明の処理方法の一例を示すフローシート、
第2図は各処理工程の配置図、第3図は本発明に用いる
クレーンの一例を示す概略図、第4図および第5図はア
ノード整備機の概略図、第6図および第7図はカソード
研磨機の概略図である。 図面中、10……クレーン、20a〜20b……電解槽、30……
アノード整備工程、40……カソード板洗浄工程、50……
カソード研磨工程、60……電着亜鉛剥離工程
FIG. 1 is a flow sheet showing an example of the processing method of the present invention,
FIG. 2 is a layout of each processing step, FIG. 3 is a schematic view showing an example of a crane used in the present invention, FIGS. 4 and 5 are schematic views of an anode maintenance machine, and FIGS. 6 and 7 are It is a schematic diagram of a cathode polisher. In the drawing, 10 …… Crane, 20a ~ 20b …… Electrolyzer, 30 ……
Anode maintenance process, 40 …… Cathode plate cleaning process, 50 ……
Cathode polishing process, 60 ... Electrodeposition zinc stripping process

フロントページの続き (72)発明者 大小田 満 秋田県秋田市茨島3−1−18 三菱金属株 式会社秋田製錬所内 (56)参考文献 特公 昭57−53437(JP,B2) 特公 昭57−53438(JP,B2) 特公 昭56−4152(JP,B2)Front Page Continuation (72) Inventor Mitsuru Oda 3-1-18 Ibaraki, Akita City, Akita Mitsubishi Metals Co., Ltd. Akita Smelter (56) References JP-B 57-53437 (JP, B2) JP-B Sho 57-53438 (JP, B2) JP-B-56-4152 (JP, B2)

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】(イ)複数の陽極板と陰極板を絶縁性の型
枠を介して交互に一定間隔ごとに一体に連結した極板ユ
ニットを形成し、該極板ユニットを電解槽に装入して電
解を行った後に、(ロ)多数の摺動自在な陽極ハンガー
と陰極ハンガーを有し、これら陽極ハンガーと陰極ハン
ガーが相互に絶縁され、各ハンガーには極板を吊下げる
フックが装着されており、該ハンガーに極板を吊下げた
状態で搬送する移送クレーンを用い、(ハ)極板ユニッ
トの各陽極板および各陰極板を移送クレーンの各ハンガ
ーに吊下げて極板ユニットを電解槽から引上げ、(ニ)
該ハンガーの移動により、各極板を吊下げた状態で互い
に引き離して極板間隔を広げ、(ホ)極板間隔を広げて
吊下げた状態で、電着金属の剥離、極板洗浄および極板
表面の研磨を含む極板処理を行い、(ヘ)極板処理後、
極板を吊り下げているハンガーを接近させて交互に配列
されている陽極板と陰極板との間隔を狭め、型枠を介し
て一定間隔に一体化して再び極板ユニットを形成して電
解工程に送ることを特徴とする電解製錬における極板処
理方法。
(A) A plurality of anode plates and a plurality of cathode plates are alternately and integrally connected to each other at regular intervals via an insulative mold to form an electrode plate unit, and the electrode plate units are mounted in an electrolytic cell. (B) Having a large number of slidable anode hangers and cathode hangers after being put in and electrolyzing, these anode hangers and cathode hangers are insulated from each other, and each hanger has a hook for hanging the electrode plate. (3) Using a transfer crane that is installed and conveys the electrode plates suspended in the hanger, (c) suspending each anode plate and each cathode plate of the electrode plate unit on each hanger of the transfer crane. From the electrolyzer, (d)
By moving the hanger, the electrode plates are pulled apart from each other to widen the electrode plate spacing, and (e) the electrode plate separation, electrode plate cleaning and After the electrode plate treatment including polishing of the plate surface, (f) after the electrode plate treatment,
The hangers that suspend the electrode plates are brought close to each other to narrow the gap between the anode plates and the cathode plates, which are alternately arranged, and they are integrated at a constant interval via a formwork to form the electrode plate unit again to perform an electrolysis process. A method for treating an electrode plate in electrolytic smelting, which comprises:
【請求項2】複数の陽極板と陰極板を同時にハンガーに
吊下げ、通電中の電解槽から極板ユニットを引上げて極
板処理工程に搬送する特許請求の範囲第1項の極板処理
方法。
2. The electrode plate treatment method according to claim 1, wherein a plurality of anode plates and cathode plates are simultaneously hung on a hanger, and the electrode plate unit is pulled up from the electrolyzing cell being energized and conveyed to the electrode plate treatment step. .
【請求項3】多数の極板をハンガーに吊下げた状態で各
極板処理手段の間を通過させる間に吊下げた多数の極板
の処理を同時に行う特許請求の範囲第1項の極板処理方
法。
3. The electrode according to claim 1, wherein the processing of a large number of suspended electrode plates is carried out at the same time while a large number of electrode plates are suspended from a hanger while passing between the electrode plate processing means. Plate processing method.
JP62096291A 1987-04-10 1987-04-21 Electrode plate treatment method in electrolytic smelting Expired - Lifetime JPH0768628B2 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
JP62096291A JPH0768628B2 (en) 1987-04-21 1987-04-21 Electrode plate treatment method in electrolytic smelting
EP88105556A EP0286093B1 (en) 1987-04-10 1988-04-07 A method for electrowinning a metal using an electrode unit consisting of assembled anode plates and cathode plates and a frame body for forming such an electrode unit
DE88105556T DE3881933T2 (en) 1987-04-10 1988-04-07 Process for the electrical extraction of metal with an electrode unit from anode and cathode plates and frame for building such an electrode unit.
CA000563645A CA1329382C (en) 1987-04-10 1988-04-08 Method for electrowinning a metal using an electrode unit consisting of assembled anode plates and cathode plates and a frame body for forming such an electrode unit
US07/179,543 US5002642A (en) 1987-04-10 1988-04-08 Method for electrowinning a metal using an electrode unit consisting of assembled anode plates and cathode plates and a frame body for forming such an electrode unit
AU14430/88A AU595996B2 (en) 1987-04-10 1988-04-08 A method for electrowinning a metal using an electrode unit consisting of assembled anode plates and a frame body for forming such an electrode unit
KR1019880004054A KR940002259B1 (en) 1987-04-10 1988-04-09 Method for electrowinning a metal using an electrode unit consisting of assembled anode plates and cathode plates and a flame body for forming such an electrode unit
FI881677A FI87659C (en) 1987-04-10 1988-04-11 Method for electrolytic extraction of a metal, frame frame for an electrode assembly and construction for assembly of anode plates and cathode plates
AU49039/90A AU625401B2 (en) 1987-04-10 1990-02-02 A frame body for forming an electrode unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62096291A JPH0768628B2 (en) 1987-04-21 1987-04-21 Electrode plate treatment method in electrolytic smelting

Publications (2)

Publication Number Publication Date
JPS63262494A JPS63262494A (en) 1988-10-28
JPH0768628B2 true JPH0768628B2 (en) 1995-07-26

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Application Number Title Priority Date Filing Date
JP62096291A Expired - Lifetime JPH0768628B2 (en) 1987-04-10 1987-04-21 Electrode plate treatment method in electrolytic smelting

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Country Link
JP (1) JPH0768628B2 (en)

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* Cited by examiner, † Cited by third party
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JPS564152A (en) * 1979-06-25 1981-01-17 Japan Carlit Co Ltd:The Elecrtrophotographic copying paper
DE3028626A1 (en) * 1980-07-29 1982-03-04 Basf Ag, 6700 Ludwigshafen METHOD FOR PRODUCING 2-ARYLOXY-ACRYLIC ACID COMPOUNDS
DE3028625A1 (en) * 1980-07-29 1982-03-04 Basf Ag, 6700 Ludwigshafen METHOD FOR PRODUCING 2-ARYLOXY-2-HALOGEN PROPIONIC ACID COMPOUNDS

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