JP2019183254A - Electrolytic slime recovery device and electrolytic slime recovery method - Google Patents

Electrolytic slime recovery device and electrolytic slime recovery method Download PDF

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JP2019183254A
JP2019183254A JP2018079380A JP2018079380A JP2019183254A JP 2019183254 A JP2019183254 A JP 2019183254A JP 2018079380 A JP2018079380 A JP 2018079380A JP 2018079380 A JP2018079380 A JP 2018079380A JP 2019183254 A JP2019183254 A JP 2019183254A
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electrolytic
slime
electrolytic slime
anode
recovery device
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JP7002008B2 (en
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佐藤 健司
Kenji Sato
健司 佐藤
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Sumitomo Metal Mining Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

To provide a device and a method for efficiently recovering an electrolytic slime generated in electrolytic refining.SOLUTION: An electrolytic slime recovery device recovers electrolytic slimes generated in a cathode, an anode arranged facing a surface of the cathode, and on a surface of the anode in an electrolytic bath for storing the electrolytic solution in which the cathode and the anode are immersed during metal electrolytic refining. The electrolytic slime recovery device comprises a removing tool which removes the electrolytic slime from the surface of the anode, and a scraper unit provided integrally with or adjacent to the removing tool and including a suction part having a suction port of the electrolytic solution containing the electrolytic slime.SELECTED DRAWING: Figure 2

Description

本発明は、銅等の金属を電解精製する際に発生する電解スライムを効率的に回収するための装置におよび電解スライム回収装置を用いた電解スライム回収方法に関する。   The present invention relates to an apparatus for efficiently recovering electrolytic slime generated when electrolytically purifying a metal such as copper, and to an electrolytic slime recovery method using an electrolytic slime recovery apparatus.

金属の精製法として電解精製法が広く用いられている。
例えば、銅の電解精製においては、銅品位99.5%程度に粗精製された銅をアノード(陽極)とし、銅品位99.99%の銅母板やステンレス母板をカソード(陰極)として、両極間に電気を通じることにより、カソード(陰極)側に銅を電着させている。
As a metal purification method, an electrolytic purification method is widely used.
For example, in the electrolytic refining of copper, copper roughly refined to a copper grade of about 99.5% is used as an anode (anode), and a copper base plate or a stainless steel base plate having a copper grade of 99.99% is used as a cathode (cathode). Copper is electrodeposited on the cathode (cathode) side by passing electricity between the two electrodes.

銅アノード中には、金、銀、鉛、ビスマスなど、銅電解における目的外金属が含まれている場合が多く、銅アノードの電解が進むにつれ、アノード表面に目的外金属が現れ、個々の溶出率に従って電解液中に溶出したり、銅アノード表面に泥状に残ったり、電解槽底に沈んで泥状の沈殿物として堆積する。前記泥状の沈殿物が電解スライムと呼ばれている。
このような電解スライムはアノード表面で層を形成することにより、目的金属の電気抵抗を高め、消費電力の増加を招き、電解効率を下げるという問題や、アノード表面から剥離された電解スライムがカソードへ付着してしまい電解後の銅の純度が低下したり、カソード表面に凹凸等の欠陥が生じる事により電気ショートが発生し生産性が低下するという問題があった。
Copper anodes often contain non-target metals such as gold, silver, lead, and bismuth in copper electrolysis. As copper anode electrolysis progresses, non-target metals appear on the anode surface, and individual elution occurs. It elutes into the electrolyte according to the rate, remains in the muddy state on the copper anode surface, or sinks to the bottom of the electrolytic cell and accumulates as a muddy precipitate. The muddy precipitate is called electrolytic slime.
Such an electrolytic slime forms a layer on the anode surface, thereby increasing the electrical resistance of the target metal, leading to an increase in power consumption, reducing the electrolytic efficiency, and the electrolytic slime peeled off from the anode surface to the cathode. There was a problem that the copper purity after electrolysis was reduced due to adhesion, or defects such as irregularities were formed on the cathode surface, resulting in an electrical short and a decrease in productivity.

上記の問題を解決するため、例えば特許文献1では陽極の表面に発生したアノード(陽極)スライムが陽極の表面から剥離する前に、陽極を電解槽から引き揚げ、アノードスライムを陽極の表面から除去した後、再び電解槽へ陽極を挿入し、電解精製を継続する電解精製方法が開示されている。   In order to solve the above problem, for example, in Patent Document 1, before the anode (anode) slime generated on the surface of the anode peels from the surface of the anode, the anode is lifted from the electrolytic cell, and the anode slime is removed from the surface of the anode. Thereafter, an electrolytic purification method is disclosed in which the anode is inserted again into the electrolytic cell and the electrolytic purification is continued.

また、特許文献2には電解精製中に、電解液に浸漬するように支持された陽極と陰極との間において、前記電解液が前記陽極の表面に対して垂直な流れを形成するように前記電解液の撹拌を実施する電解精製装置が開示されている。
特許文献2の発明では極板間において陽極に向かう電解液が陽極表面に対して垂直な流れを形成することにより、陰極へのスライムへの付着を抑制しつつ、陽極表面における銅イオンの溶出を促進することができる。
Patent Document 2 discloses that the electrolytic solution forms a flow perpendicular to the surface of the anode between the anode and the cathode supported so as to be immersed in the electrolytic solution during electrolytic purification. An electrolytic purification apparatus that performs stirring of an electrolytic solution is disclosed.
In the invention of Patent Document 2, the electrolyte flowing toward the anode between the electrode plates forms a flow perpendicular to the anode surface, thereby suppressing elution of copper ions on the anode surface while suppressing adhesion of slime to the cathode. Can be promoted.

特許文献3では電解槽中に吊り下げられたカソードの下端よりも下方の供給口から各カソードへ向けてそれぞれ電解液を供給するとともに、前記電解槽の上部に設けた電解液排出口からオーバーフローする電解液を排出して、前記電解槽内の電解液を循環させる電解精製方法が開示されている。
特許文献3の発明ではカソードにスライムが付着することを抑止するとともに、各カソードに対する添加剤の供給のばらつきを無くして、凹凸の少ない高品位の金属を精製できるとされている。
In Patent Document 3, an electrolyte is supplied to each cathode from a supply port below a lower end of a cathode suspended in an electrolytic cell, and overflows from an electrolyte discharge port provided in the upper part of the electrolytic cell. An electrolytic purification method is disclosed in which the electrolytic solution is discharged and the electrolytic solution in the electrolytic cell is circulated.
In the invention of Patent Document 3, it is said that slime can be prevented from adhering to the cathode, and variation in the supply of the additive to each cathode can be eliminated, so that a high-quality metal with few irregularities can be purified.

これらの特許文献1〜3に記載の方法では、アノード表面で発生する電解スライム、そのものを、電解槽から排除するものではなく、発生した電解スライムは、アノード表面から剥離して電解槽底面に堆積した後は、可能な限り電解液内を舞い上がらせずに電解精製終了まで維持することが行われてきていた。   In the methods described in Patent Documents 1 to 3, the electrolytic slime generated on the anode surface itself is not excluded from the electrolytic cell, but the generated electrolytic slime is peeled off from the anode surface and deposited on the bottom of the electrolytic cell. After that, it has been carried out to keep the electrolytic solution as far as possible without raising the electrolytic solution.

特開2005−187833号公報JP 2005-187833 A 特開2017−048438号公報JP 2017-048438 A 特開2017−057508号公報JP 2017-057508 A

しかしながら、本発明では、上記のような従来事情に鑑み、電解槽から積極的に、この電解スライムを、その電解精製稼働中においても、電解液を必要以上には撹乱せずに、且つカソード表面の清浄性を維持しながら、排除することに着目し、本発明に至ったものである。
本発明は、電解精製において発生する電解スライムを効率的に回収するための装置及び電解スライム回収方法を提供する。
However, in the present invention, in view of the above-described conventional circumstances, the electrolytic slime is actively removed from the electrolytic cell without disturbing the electrolytic solution more than necessary even during the electrolytic refining operation. Focusing on the elimination while maintaining the cleanliness of the present invention, the present invention has been achieved.
The present invention provides an apparatus and an electrolytic slime recovery method for efficiently recovering electrolytic slime generated in electrolytic purification.

本発明の第1の発明は、金属の電解精製時に、カソードと前記カソード表面と対向して配置されるアノードと、前記カソード及びアノードが浸漬している電解液を貯留した電解槽における前記アノード表面に発生する電解スライムの回収装置であって、前記アノード表面の前記電解スライムを、前記アノード表面から除去する除去具と、前記除去具と一体若しくは隣接して設けられ、前記電解スライムを含んだ電解液の吸引口を有する吸引部を含むスクレイバー部を備えることを特徴とする電解スライム回収装置である。   According to a first aspect of the present invention, there is provided a cathode, an anode disposed opposite to the cathode surface, and an anode surface in an electrolytic cell storing an electrolyte in which the cathode and the anode are immersed during electrolytic refining of metal. A device for collecting the electrolytic slime generated in the anode, the removing device for removing the electrolytic slime on the anode surface from the anode surface, and the electrolytic device including the electrolytic slime provided integrally with or adjacent to the removing device. An electrolytic slime recovery apparatus comprising a scraper portion including a suction portion having a liquid suction port.

本発明の第2の発明は、第1の発明におけるスクレイバー部が、前記除去具が配置されたアノードと対向した位置のカソードの表面に近接した位置、且つ略平行な位置に配置される隔壁を有することを特徴とする電解スライム回収装置である。   According to a second aspect of the present invention, there is provided a partition wall in which the scraper portion according to the first aspect is disposed at a position close to and substantially parallel to the surface of the cathode facing the anode on which the removal tool is disposed. It is an electrolysis slime recovery device characterized by having.

本発明の第3の発明は、第1の発明における吸引部により吸引された電解スライムを含んだ電解液から、前記電解スライムを分離して濾過後電解液を生成し、分離した前記電解スライムを回収する電解スライム回収部と、前記濾過後電解液を、前記電解槽に循環供給する供給部を備えることを特徴とする電解スライム回収装置である。   According to a third aspect of the present invention, the electrolytic slime is separated from the electrolytic solution containing the electrolytic slime sucked by the suction portion in the first invention to produce an electrolytic solution after filtration, and the separated electrolytic slime is An electrolytic slime recovery device comprising: an electrolytic slime recovery unit to be recovered; and a supply unit that circulates and supplies the filtered electrolyte solution to the electrolytic cell.

本発明の第4の発明は、第3の発明における電解スライム回収部が、電解スライムを含んだ電解液から、前記電解スライムを濾し取り、回収電解スライムと濾過後電解液に分離する浄液フィルタを有することを特徴とする電解スライム回収装置である。   A fourth aspect of the present invention is a liquid purification filter in which the electrolytic slime recovery section in the third aspect filters the electrolytic slime from the electrolytic solution containing electrolytic slime and separates it into the recovered electrolytic slime and the filtered electrolytic solution It is an electrolysis slime recovery device characterized by having.

本発明の第5の発明は、第3及び第4の発明における供給部が、前記除去具が配置されたアノードと対向した位置のカソードの表面に近接した位置、且つ略平行な位置に配置される隔壁とカソード間に、前記濾過後電解液を放出する供給口を有することを特徴とする電解スライム回収装置である。   According to a fifth aspect of the present invention, the supply unit according to the third and fourth aspects is disposed at a position close to and substantially parallel to the surface of the cathode at a position facing the anode where the removal tool is disposed. An electrolytic slime recovery device having a supply port for discharging the electrolytic solution after filtration between a partition wall and a cathode.

本発明の第6の発明は、第1から第5の発明における除去具の配置が、逆V字構造であることを特徴とする電解スライム回収装置である。   According to a sixth aspect of the present invention, there is provided the electrolytic slime recovery apparatus, wherein the arrangement of the removal tool in the first to fifth aspects has an inverted V-shaped structure.

本発明の第7の発明は、第1から第6の発明における電解スライム回収装置を、電解槽上方に吊り下げた状態から、電解槽内における前記回収装置の設置箇所に配置する際に、前記電解槽に貯留された電解液に前記回収装置の吸引部が浸漬した時点から順次、アノード表面の電解スライムの除去処理と、アノード表面近傍の電解スライムを含む電解液の吸引と、カソード表面近傍への電解液の供給を開始することを特徴とする電解スライム回収方法である。   According to a seventh aspect of the present invention, when the electrolytic slime recovery device according to the first to sixth aspects of the present invention is disposed at a location where the recovery device is installed in the electrolytic cell from a state suspended above the electrolytic cell, From the time when the suction part of the recovery device is immersed in the electrolytic solution stored in the electrolytic cell, the electrolytic slime removal treatment on the anode surface, the suction of the electrolytic solution containing electrolytic slime near the anode surface, and the vicinity of the cathode surface The electrolytic slime recovery method is characterized in that the supply of the electrolytic solution is started.

本発明の第8の発明は、少なくとも偶数基の第1から第6の発明における電解スライム回収装置を用い、前記電解スライム回収装置をナンバリングし、前記電解スライム回収装置の2基を対とし、アノード両面に各1基が設置されるように配置し、前記電解スライム回収装置の除去具及び吸引口を前記電解液中に液没させながら、前記電解スライム回収装置の前記除去具による電解スライムの除去処理と、アノード表面近傍の電解スライムを含む電解液の吸引と、カソード表面近傍への電解液の供給を、奇数番目と偶数番目の電解スライム回収装置を交互動作させてアノード表面に発生する電解スライムを含む電解液を回収することを特徴とする電解スライム回収方法である。   According to an eighth aspect of the present invention, there is provided an electrolytic slime recovery device according to the first to sixth inventions of at least an even number group, the electrolytic slime recovery device is numbered, and two groups of the electrolytic slime recovery device are paired, and the anode Removal of electrolytic slime by means of the removal tool of the electrolytic slime recovery device is arranged so that one unit is installed on each side, and the removal tool and suction port of the electrolytic slime recovery device are immersed in the electrolytic solution. Electrolytic slime generated on the anode surface by alternately operating odd-numbered and even-numbered electrolytic slime recovery devices for treatment, suction of electrolytic solution containing electrolytic slime near the anode surface, and supply of electrolytic solution near the cathode surface An electrolytic slime recovery method characterized by recovering an electrolytic solution containing

本発明の第9の発明は、電解精製の稼働中に第7及び第8の発明における電解スライム回収装置を用いてアノード表面に発生する電解スライムを回収することを特徴とする電解スライム回収方法である。   The ninth invention of the present invention is an electrolytic slime recovery method characterized in that the electrolytic slime generated on the anode surface is recovered using the electrolytic slime recovery device in the seventh and eighth inventions during the operation of electrolytic purification. is there.

本発明の第10の発明は、第7から第9の発明における電解スライム回収装置に設置された除去具を電解槽上部に、除去具部分を下方に向けて吊り下げた状態から、前記除去具を電解槽底方向に移動させ、前記除去具が電解槽に貯留された電解液中に全没した後に、電解スライム回収装置の交互動作を開始することを特徴とする電解スライム回収方法である。   According to a tenth aspect of the present invention, there is provided the remover from a state in which the remover installed in the electrolytic slime recovery device according to the seventh to ninth aspects is suspended from the upper part of the electrolytic cell and the remover part downward. Is moved to the bottom of the electrolytic cell, and after the removal tool is completely submerged in the electrolytic solution stored in the electrolytic cell, an alternate operation of the electrolytic slime recovery device is started.

本発明の電解スライム回収装置を用いた電解スライム回収方法によれば、アノード表面に残存する電解スライムを効率的に回収できると共に、カソード表面の清浄性を維持しつつ、電解精製の効率を著しく向上することが可能となる。   According to the electrolytic slime recovery method using the electrolytic slime recovery apparatus of the present invention, the electrolytic slime remaining on the anode surface can be efficiently recovered, and the efficiency of electrolytic purification is significantly improved while maintaining the cleanliness of the cathode surface. It becomes possible to do.

電解槽の構成を説明する側面図である。It is a side view explaining the structure of an electrolytic vessel. 本発明に係る電解スライムの回収装置の概略構成図である。It is a schematic block diagram of the collection device of the electrolytic slime concerning the present invention. (a)本発明に係る除去部の一実施例を示す構成図で、(b)本発明の他の実施例を示す構成図で、(c)本発明の他の実施例を示す構成図である。(A) It is a block diagram which shows one Example of the removal part which concerns on this invention, (b) It is a block diagram which shows the other Example of this invention, (c) It is a block diagram which shows the other Example of this invention. is there. 本発明に係る吸引部の他の例を示す概略構成図である。It is a schematic block diagram which shows the other example of the suction part which concerns on this invention. 本発明に係るスクレイバー部を示す概略模式図で、(a)はブラシ型の除去具を持つ別体型のスクレイバー部の一例、(b)はブラシ型の除去具を持つ一体型のスクレイバー部の一例、(c)は、たわし型の除去具を持つ別体型のスクレイバー部の例、(d)はヘラ型の除去具を持つ一体型のスクレイバー部の一例を示す図である。BRIEF DESCRIPTION OF THE DRAWINGS It is a schematic diagram which shows the scraper part which concerns on this invention, (a) is an example of a separate type | mold scraper part with a brush-type removal tool, (b) is an example of an integrated type scraper part with a brush-type removal tool. (C) is a figure which shows an example of the separate type | mold scraper part which has a scouring-type removal tool, (d) is a figure which shows an example of an integrated type scraper part which has a spatula-type removal tool. 本発明に係る供給部の概略構成図で、(a)は側面側からの供給部の電解液に浸漬された直後の状態を示す図、(b)は上方からの図、(c)は回収作業中の供給部の状態を示す図である。BRIEF DESCRIPTION OF THE DRAWINGS It is a schematic block diagram of the supply part which concerns on this invention, (a) is a figure which shows the state immediately after being immersed in the electrolyte solution of the supply part from the side, (b) is a figure from upper direction, (c) is collection | recovery. It is a figure which shows the state of the supply part in work. 本発明に係る電解スライム回収方法の説明図で、(a)は、回収装置の電解液浸漬直後の状態を示す図で、(b)は、電解スライム回収中の図である。(c)は、回収装置を上下に交互動作される運転機構の一例を示す図である。It is explanatory drawing of the electrolytic slime collection | recovery method based on this invention, (a) is a figure which shows the state immediately after electrolyte solution immersion of a collection | recovery apparatus, (b) is a figure during electrolytic slime collection | recovery. (C) is a figure which shows an example of the driving | operation mechanism by which a collection | recovery apparatus is alternately operated up and down.

本発明の実施形態について図面を参照しながら説明する。
図1は本発明の電解スライム回収装置が用いられる電解槽の構成を説明する側面断面図である。
電解槽1内には、電解液2が溜められ、その電解液2中にアノード3とカソード4が一定の間隔で交互に浸漬されている。
通常、使用するアノード3としては精製する金属の原料金属が用いられる。例えば銅精製の場合は銅品位99.5%程度の粗銅が用いられる。
一方、カソード4としては、純銅板やステンレス板が用いられる。
電解液2として硫酸酸性の硫酸銅水溶液が用いられている。
Embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a side sectional view for explaining the configuration of an electrolytic cell in which the electrolytic slime recovery apparatus of the present invention is used.
An electrolytic solution 2 is stored in the electrolytic cell 1, and anodes 3 and cathodes 4 are alternately immersed in the electrolytic solution 2 at regular intervals.
Usually, as the anode 3 to be used, a raw material metal of a metal to be purified is used. For example, in the case of copper purification, crude copper having a copper grade of about 99.5% is used.
On the other hand, as the cathode 4, a pure copper plate or a stainless steel plate is used.
As the electrolytic solution 2, an acidic copper sulfate aqueous solution is used.

電解精製が行われている間、アノード表面には電解スライムと呼ばれるアノードに含まれる不純物を主とする流動性の塊、ノロが発生し、電解液中に拡散すると、電解液を汚すことになり、結果として電解精製の生成物であるカソードの品質を低下させてしまうと同時に、電解効率を低下させる原因となっている。そこで、従来は、その電解スライムが発生した後は、電解液内で静置状態を維持する方策がおこなわれてきたが、本発明では、そのような電解スライムをアノード表面から積極的に除去する方策を見出し、完成に至ったものが、本発明に係る電解スライム回収装置である。   While electrolytic refining is being performed, a fluid mass, mainly roasting impurities contained in the anode, called electrolytic slime, is generated on the anode surface, and if it diffuses into the electrolyte, it will contaminate the electrolyte. As a result, the quality of the cathode, which is a product of electrolytic purification, is lowered, and at the same time, the electrolytic efficiency is lowered. Thus, conventionally, after the generation of the electrolytic slime, measures have been taken to maintain the stationary state in the electrolytic solution, but in the present invention, such electrolytic slime is positively removed from the anode surface. What has been found and completed is the electrolytic slime recovery device according to the present invention.

図2は本発明に係る電解スライム回収装置の構成を説明する図で、100は本発明に係る電解スライム回収装置で、Aは電解スライム除去部、Bは電解スライム回収部、Cは供給部、Sはスクレイバー部、5は電解スライムの除去具、6は吸引口、7は吸引部、8は浄液フィルタ、8aは濾過ポット、9は輸送管、10は供給口、bは開閉弁、hは隔壁、Pは送液ポンプである。 FIG. 2 is a diagram for explaining the configuration of an electrolytic slime recovery apparatus according to the present invention, in which 100 is an electrolytic slime recovery apparatus according to the present invention, A is an electrolytic slime removal unit, B is an electrolytic slime recovery unit, C is a supply unit, S is a scraper part, 5 is an electrolytic slime removal tool, 6 is a suction port, 7 is a suction part, 8 is a liquid filter, 8a is a filtration pot, 9 is a transport pipe, 10 is a supply port, b is an on-off valve, h partition wall, P 1 is a liquid feed pump.

図2に示す電解スライム回収装置100は、電解スライムを掻き取る除去具5(例えば図中のブラシなど)と、その除去具により掻き取られた電解スライムを電解液と共に吸引する吸引口6と電解スライム吸引時にカソード表面への影響を抑える隔壁hを有する吸引部7からなるスクレイバー部Sと輸送管などの付帯設備で構成される電解スライム除去部Aと、吸引された電解スライムを含んだ電解液から、電解スライムを分離して濾過後電解液を生成し、分離した電解スライムを回収する電解スライム回収部Bと、濾過後電解液を送液ポンプで電解槽に電解液として循環供給する供給部Cとに大別される。
以下、各部を順に説明する。なお、図2において、黒矢印は電解スライムを含む電解液、破線矢印は濾過後の電界液の流れを示すものである。
An electrolytic slime recovery apparatus 100 shown in FIG. 2 includes a removal tool 5 (for example, a brush in the figure) that scrapes the electrolytic slime, a suction port 6 that sucks the electrolytic slime scraped by the removal tool together with the electrolytic solution, and electrolysis. Electrolytic slime removing part A composed of a scraper part S having a partition wall h having a partition wall h that suppresses the influence on the cathode surface during slime suction and ancillary equipment such as a transport pipe, and an electrolytic solution containing the sucked electrolytic slime The electrolytic slime is separated to produce an electrolytic solution after filtration and the separated electrolytic slime is collected, and the supply unit that circulates and supplies the filtered electrolytic solution to the electrolytic cell as an electrolytic solution with a liquid feed pump It is roughly divided into C.
Hereinafter, each part is demonstrated in order. In FIG. 2, the black arrow indicates the electrolytic solution containing electrolytic slime, and the broken line arrow indicates the flow of the electrolytic solution after filtration.

[電解スライム除去部]
この電解スライム除去部Aにおける主要部位であるスクレイバー部Sは、アノード表面に接触するように配置され、電解精製中にアノード表面に発生する電解スライムをアノード表面から掻き取るためのブラシのような除去具5と、その除去具5の上方に除去具5によって掻き取られた電解スライムを電解液と一緒に吸引するための吸引口6を有する吸引部7が、除去具5と一体若しくは連結して設けられている。この除去具5と吸引部7は一体となって、除去具5がアノード表面と接触状態を維持しながら、移動することで、除去具5がアノード表面の電解スライムを掻き取り、アノード表面から浮かせ、その浮いた電解スライムを吸引口6から吸い取り、アノード表面から除去する役割を有している。
さらに、アノード表面から掻き取られ、電解液中に浮遊状態の電解スライムが、カソード表面に付着して汚染するのを防ぐ役割を果たす隔壁hが、掻き取り作業が行われているアノード3の表面と、そのアノード3の表面に対向した位置にあるカソード4の表面に近接した位置、且つ略平行な位置に配置されている。
[Electrolytic slime removal section]
The scraper part S, which is the main part in the electrolytic slime removing part A, is disposed so as to contact the anode surface, and is removed like a brush for scraping the electrolytic slime generated on the anode surface during electrolytic purification from the anode surface. A suction part 7 having a suction port 6 for sucking together with the electrolyte 5 the electrolytic slime scraped by the removal tool 5 above the removal tool 5 is integrally or connected to the removal tool 5. Is provided. The removal tool 5 and the suction part 7 are integrated, and the removal tool 5 moves while maintaining contact with the anode surface, so that the removal tool 5 scrapes off the electrolytic slime on the anode surface and lifts it from the anode surface. The floated electrolytic slime is sucked from the suction port 6 and removed from the anode surface.
Further, the partition wall h that is scraped off from the anode surface and serves to prevent the electrolytic slime floating in the electrolytic solution from adhering to the cathode surface and contaminating the surface of the anode 3 on which the scraping operation is performed. And a position close to and substantially parallel to the surface of the cathode 4 at a position facing the surface of the anode 3.

その形態は、図3(a)〜(c)に示されるような構造を採用することができる。
図3(a)は、アノードの幅より短い長さ(例えば、1/10〜1/5程度)を持つ除去具5とその上方に設置された吸引口6を備える吸引部7からなるユニットを単独で装備する形態のものである。なお、本ユニットを複数用い、アノード幅一杯に配置して用いても良い。なお、図中の黒矢印は、スクレイバー部の動作軌跡を示している。
図3(b)は、アノード幅とほぼ同じ長さを持つ除去具5を有し、その上方に吸引口6を配置した構成の吸引部7からなるユニットを装備した形態のものである。なお図中の白抜き矢印は、スクレイバー部の動作軌跡を示している。
図3(c)は、逆V字状の除去具5を単独又は複数有し、その上方に吸引口6を備えた吸引部からなるユニットを装備した形態を示している。なお図中の白抜き矢印は、スクレイバー部の動作軌跡を示している。
また、図3(a)〜(c)は、いずれもアノードからカソード方向を視認した場合の各構成要素の配置を示した図となっている。
The form can employ | adopt a structure as shown to Fig.3 (a)-(c).
FIG. 3A shows a unit composed of a removal unit 5 having a length shorter than the width of the anode (for example, about 1/10 to 1/5) and a suction unit 7 including a suction port 6 disposed above the removal tool 5. It is in the form of being equipped alone. Note that a plurality of the units may be used and arranged so as to fill the anode width. In addition, the black arrow in a figure has shown the operation | movement locus | trajectory of the scraper part.
FIG. 3B shows a configuration in which a removal tool 5 having substantially the same length as the anode width is provided, and a unit including a suction portion 7 having a suction port 6 disposed thereon is provided. In addition, the white arrow in a figure has shown the operation | movement locus | trajectory of the scraper part.
FIG. 3C shows a form in which a unit including a suction part having a single or a plurality of inverted V-shaped removal tools 5 and having a suction port 6 above is provided. In addition, the white arrow in a figure has shown the operation | movement locus | trajectory of the scraper part.
FIGS. 3A to 3C are diagrams showing the arrangement of each component when the direction from the anode to the cathode is visually recognized.

なお、吸引部は除去具に向かって末広がりの開口(吸引口)を持つラッパ状の筐体を持ち、通常吸引口と対向した位置に、吸引した電解スライムを含んだ電解液を回収部に運ぶ輸送管9を備え、この輸送管9は送液ポンプPと繋がっている(図2参照)。
また、図4に見られるように、上下に少なくとも2個のスクレイバー部S、Sを備える構成であっても良い。
複数のスクレイバー部S、Sを吸引部が備える場合、各スクレイバー部から吸引部への輸送管9、9に、開閉弁b、bを設けることで、電解スライムの掻き取り作業及び吸引作業をスクレイバー部毎に独立して制御可能となり、例えば、電解液に浸漬する際には、電解液への浸漬タイミングにより開閉弁bを開位置とし、開閉弁bを閉位置として、スクレイバー部Sを先ず稼働させ、電解スライムの回収作業を行いながら、電解槽底部方向に移動していく。
さらに、スクレイバー部Sの電解液への浸漬と同期して、開閉弁bが開位置となり、スクレイバー部Sによる電解スライムの回収作業が開始される。このスクレイバー部Sが稼働した状態では、開閉弁bを閉じて、スクレイバー部Sの動作を中断しても、そのままの継続状態であっても良く、電解液の状態や電解スライム発生状況やカソード表面状態などを考慮して判断する。
The suction part has a trumpet-shaped housing with an opening (suction port) spreading toward the removal tool, and the electrolyte containing the sucked electrolytic slime is conveyed to the recovery unit at a position facing the normal suction port. comprising a transport pipe 9, the transport pipe 9 is connected to the liquid feed pump P 1 (see FIG. 2).
Moreover, as seen in FIG. 4, vertically it may be configured to include at least two Sukureiba portion S 1, S 2.
When a suction part is provided with a plurality of scraper parts S 1 and S 2 , an electrolysis slime scraping operation can be performed by providing on-off valves b 1 and b 2 in transport pipes 9 and 9 from each scraper part to the suction part. the suction working independently for each Sukureiba unit enables control, for example, when immersed in the electrolyte, the on-off valve b 2 and an open position, the opening and closing valve b 1 as the closed position by immersion timing to the electrolyte, first operate the Sukureiba section S 2, while recovery operations electrolysis slime, moves to the electrolytic cell bottom direction.
Further, in synchronization with the immersion in the electrolytic solution Sukureiba section S 1, the opening and closing valve b 1 is in an open position, recovery operations electrolytic slime by Sukureiba portion S 1 is being started. In a state where the Sukureiba portion S 1 is the operation, close the shutoff valve b 2, even interrupt the operation of Sukureiba section S 2, it may be intact continuation state, the electrolyte status and electrolytic slime occurrence And the cathode surface condition.

除去具5の形態は、一般的なデッキブラシ、洗車ブラシ、整髪ブラシのような毛先の一端が拘束されたブラシ形状のものを想定しているが、コイル形態やたわし形態などの、アノード表面の電解スライムを、アノード表面を傷付けずに掻き取ることが可能な形態であることが重要であり、さらには、ブラシの柄を中空とし、ブラシの毛先基部の柄部分に電解スライムを吸い取り可能な程度の空孔を設けたブラシでは、吸引口を併せて備えることが可能な形態である。さらに、ガラスワイパーのようなT字形形状で、且つ先端のT字部が樹脂で構成され、その部位で電解スライムを掻き取るタイプの除去具も使用可能である。   The shape of the removal tool 5 is assumed to be a brush shape in which one end of a hair tip is constrained, such as a general deck brush, a car wash brush, and a hairstyling brush. It is important that the electrolytic slime can be scraped off without damaging the anode surface. Furthermore, the brush handle is hollow, and the electrolytic slime can be absorbed into the handle portion of the brush tip base. In a brush provided with a certain amount of holes, it is possible to provide a suction port together. Further, it is possible to use a removal tool of a T-shaped shape such as a glass wiper, the T-shaped portion at the tip of which is made of resin, and scraping the electrolytic slime at that portion.

図5に、上記除去具を含めたスクレイバー部の実施例を示す。
図5(a)のスクレイバー部Saは、ブラシ型の除去具5aと、吸引口6及び吸引部7が隣接した別体のスクレイバー部を構成している。図5(b)は、柄が中空の洗車ブラシ型のスクレイバー部Sbで、ブラシ型の除去具5aと吸引口6、吸引部7が一体の構成物の例である。図5(c)は、除去具がたわし型の除去具5bを備えた別体型のスクレイバー部Scである。図5(d)は、T字形のガラスワイパーのような形状を持つスクレイバー部Sdで、除去具は樹脂製のへら5cをT字部に備え、T字形部材を吸引部7とし、その吸引部6に吸引口6が設けられた一体型のスクレイバー部Sdである。
なお、図5内の白抜き矢印は、吸引された電解スライムを含んだ電解液の流れる方向を示している。
FIG. 5 shows an example of the scraper unit including the removal tool.
The scraper portion Sa in FIG. 5A constitutes a separate scraper portion in which the brush-type removal tool 5a, the suction port 6 and the suction portion 7 are adjacent to each other. FIG. 5B is an example of a car wash brush-type scraper portion Sb having a hollow handle, in which the brush-type removal tool 5a, the suction port 6, and the suction portion 7 are integrated. FIG. 5 (c) shows a separate-type scraper portion Sc provided with a scouring-type removing tool 5b. FIG. 5 (d) shows a scraper portion Sd having a shape like a T-shaped glass wiper. The removing tool includes a resin spatula 5c in the T-shaped portion, and the T-shaped member is a suction portion 7, and the suction portion. 6 is an integrated scraper portion Sd provided with a suction port 6.
In addition, the white arrow in FIG. 5 has shown the direction through which the electrolyte solution containing the attracted electrolytic slime flows.

このような除去具5の材質は、アノード表面を深く傷つけず、且つ電解液に侵されない材質であれば金属、卑金属の区別なく種々の材質を用いることができるが、例えば、耐酸性を有し、アノード表面を傷つけない材質としてはポリプロピレン(PP)や塩化ビニル(PVC)等の有機高分子材料が好適に用いることができる。   As the material of the removal tool 5, various materials can be used without distinction between metal and base metal as long as the material does not deeply damage the anode surface and is not attacked by the electrolyte solution. As a material that does not damage the anode surface, an organic polymer material such as polypropylene (PP) or vinyl chloride (PVC) can be suitably used.

[電解スライム回収部]
この電解スライム回収部Bでは、吸引された電解スライムを含んだ電解液を、電解スライム(若干の電解液を含む)と、濾過後電解液として汚れの少ない電解液に分離し、電解スライムの回収と、濾過後電解液を供給部に送液する役割を担っている。
[Electrolytic slime recovery section]
In this electrolytic slime recovery part B, the electrolytic solution containing the sucked electrolytic slime is separated into an electrolytic slime (including some electrolytic solution) and an electrolytic solution with less dirt as a filtered electrolytic solution, and the electrolytic slime is recovered. And it plays the role which sends the electrolyte solution after filtration to a supply part.

図2に示す、その具体的な構成は、電解スライムを含んだ電解液から、電解スライムを濾し取り、回収電解スライムと濾過後電解液に分離する浄液フィルタ8と、濾過後電解液を一時的に貯留する濾過ポット8aからなる。なお、浄液フィルタ8で分離された電解スライムは、浄液フィルタ8にある程度貯まった状態で、浄液フィルタの交換や電解スライムの除去作業などの廃棄処理が行われて電解槽内から系外に排出される。   The specific configuration shown in FIG. 2 is that the electrolytic slime is filtered from the electrolytic solution containing the electrolytic slime and separated into the recovered electrolytic slime and the filtered electrolytic solution, and the filtered electrolytic solution is temporarily used. It consists of the filtration pot 8a which stores automatically. The electrolytic slime separated by the liquid purification filter 8 is stored in the liquid purification filter 8 to some extent, and is subjected to disposal processing such as replacement of the liquid purification filter and removal of the electrolytic slime from the inside of the electrolytic cell. To be discharged.

[供給部]
供給部Cは、図2又は図6に示すように、アノード3とはスクレイバー部Sを介して対向した位置で、そのアノード3の隣り合うカソード4の表面に近接した位置、且つ略平行な位置に配置される隔壁hとカソード4間に、濾過後電解液を放出する供給口10を有している。また、その供給口10は輸送管9を通じて浄液フィルタ8の濾過後電解液側に繋がり、送液ポンプPにより濾過後電解液が、電解スライムの除去を行っているアノード近傍のカソード表面に向かって送液され、供給口10から電解槽に循環されている。なお、隔壁hを用いない場合には、濾過後電解液の供給口10は、カソード上部の表面近傍で、濾過後電解液を緩やかに放出できる、即ち、カソード表面に対して層流の性質を有する流れになるように放出可能な位置、及び条件で放出される。
[Supply section]
As shown in FIG. 2 or FIG. 6, the supply part C is a position facing the anode 3 via the scraper part S, a position close to the surface of the cathode 4 adjacent to the anode 3, and a substantially parallel position. Between the partition wall h and the cathode 4, which are disposed in the same, a supply port 10 for discharging the electrolytic solution after filtration is provided. Further, the supply port 10 is connected to the filtration after the electrolysis solution side of the solution purification filter 8 through transport pipe 9, the electrolytic solution filtered by the liquid feed pump P 1 is the cathode surface of the anode near doing removal of electrolysis slime The liquid is fed toward the electrolytic cell from the supply port 10. When the partition wall h is not used, the post-filter electrolyte supply port 10 can gently release the post-filter electrolyte near the surface of the upper part of the cathode, that is, has a laminar flow property with respect to the cathode surface. It is discharged at a position where it can be discharged so as to have a flow and conditions.

図6に、電解槽内での供給部Cの形態を示す。(a)は側面側からの供給部の電解液に浸漬された直後の状態を示す側面模式図で、(b)は上方から電解槽上面の状態を示す上面模式図で、(c)は回収作業中の供給部の状態を示す側面模式図で、スクレイバー部Sがアノードの電解槽底方向の先端部にある場合を示している。なお、図6では電解槽における電解精製の一ユニットを示して説明しているもので、電解槽内では複数の図6に示す状態が設定されている。   In FIG. 6, the form of the supply part C in an electrolytic cell is shown. (A) is a schematic side view showing a state immediately after being immersed in the electrolyte solution of the supply unit from the side, (b) is a schematic top view showing the state of the upper surface of the electrolytic cell from above, and (c) is a recovery. It is a side surface schematic diagram which shows the state of the supply part in operation | work, and has shown the case where the scraper part S exists in the front-end | tip part of the electrolytic cell bottom direction of an anode. FIG. 6 shows and describes one unit of electrolytic purification in the electrolytic cell, and a plurality of states shown in FIG. 6 are set in the electrolytic cell.

通常、電解スライム回収装置は、その2基のスクレイバー部S(奇数基)と、Sn+1(偶数基)を、電解スライムの除去処理を行うアノード3を介して、その表面に設置される。また、そのアノード3と隣り合うカソード4、4との間には、掻き取った電解スライムで汚された電解液による悪影響を避けるための隔壁h、hが設けられる。その隔壁hとカソード4との間には、電解液の汚れの影響を極力抑えるために放出される濾過後電解液の供給口10が設置されている。この供給口10は、電解液が放出されることで電解スライムがカソード表面側に寄りつくのを防ぐために、少なくともカソードの電解槽底方向における中央部位置以下には配置されないように、回収部Bとは同期しながら別個に制御されている。図中の破線矢印は放出される電解液の流れの一部を示している。また、実線矢印は、吸引された電解スライムを含む電解液の流れ方向を示している。
なお、各部に設けられた送液用のポンプの形態は、図に示す構成に拘束されるものではなく、適宜望ましい構成を採用することができる。また、図中の白抜き矢印は、電解スライム除去部の上下動の動作を示すもので、横動の動作は紙面垂直方向になる。
Usually, the electrolytic slime recovery apparatus is installed on the surface of the two scraper portions S n (odd number group) and S n + 1 (even number group) via the anode 3 that performs electrolytic slime removal treatment. Further, partition walls h and h are provided between the anode 3 and the adjacent cathodes 4 and 4 in order to avoid an adverse effect due to the electrolytic solution soiled with the scraped electrolytic slime. Between the partition wall h and the cathode 4, a post-filtered electrolyte solution supply port 10 is disposed in order to suppress the influence of the electrolyte solution contamination as much as possible. In order to prevent electrolytic slime from leaning toward the cathode surface due to the discharge of the electrolytic solution, the supply port 10 is not disposed at least below the central position in the electrolytic cell bottom direction of the cathode so that the recovery unit B And are controlled separately in synchronization. Broken line arrows in the figure indicate a part of the flow of the electrolyte solution to be discharged. Moreover, the solid line arrow has shown the flow direction of the electrolyte solution containing the attracted electrolytic slime.
In addition, the form of the pump for liquid feeding provided in each part is not restrained by the structure shown to a figure, and can employ | adopt a desirable structure suitably. Also, the white arrow in the figure indicates the vertical movement operation of the electrolytic slime removal unit, and the horizontal movement is in the direction perpendicular to the page.

次に、本発明の電解スライムの回収装置を用いた電解スライムの回収方法を説明する。
図7は本発明に係る電解スライム回収方法の説明図で、(a)は、回収装置の電解液浸漬直後の状態を示す図で、(b)は、電解スライム回収中の図である。(c)は、回収装置を上下に交互動作される運転機構の一例を示す図である。
本発明に係る電解スライム回収装置を、電解槽上方に吊り下げた状態から、電解槽内の回収装置設置位置に配置する際に、図7(a)に示されるように、先ず隔壁hが電解槽に貯留された電解液2に浸漬された後、隔壁hを他の部位より先行させて電解槽底部方向に配置して他の部位の浸漬、電解スライムの回収作業を行う、或いは隔壁配置位置(通常アノードの電解槽底側先端部より電解槽底部側に設定されている)に、他の部位に先行して配置した後に、回収装置の他の部位の浸漬した部分から順次、電解スライムの回収作業であるアノード表面近傍の電解スライムを含む電解液の吸引と、カソード表面近傍への電解液の供給を開始する。
Next, an electrolytic slime recovery method using the electrolytic slime recovery apparatus of the present invention will be described.
FIG. 7 is an explanatory view of an electrolytic slime recovery method according to the present invention. FIG. 7 (a) is a diagram showing a state immediately after immersion of the electrolytic solution in the recovery device, and FIG. 7 (b) is a diagram during recovery of electrolytic slime. (C) is a figure which shows an example of the driving | operation mechanism by which a collection | recovery apparatus is alternately operated up and down.
When the electrolytic slime recovery device according to the present invention is placed from the state suspended above the electrolytic cell at the recovery device installation position in the electrolytic cell, first, as shown in FIG. After being immersed in the electrolytic solution 2 stored in the tank, the partition wall h is preceded by another part and arranged in the direction of the bottom of the electrolytic tank, so that the other part is immersed, the electrolytic slime is recovered, or the partition wall is disposed. (Normally set at the bottom of the electrolyzer from the top of the electrolyzer bottom side of the anode) After placing in front of the other parts, sequentially from the immersed part of the other parts of the recovery device, The suction of the electrolytic solution containing the electrolytic slime in the vicinity of the anode surface and the supply of the electrolytic solution to the vicinity of the cathode surface are started.

その際には、少なくとも2基のナンバリングした電解スライム回収装置を用い、その電解スライム回収装置の2基を対とし、アノード両面に各1基が設置されるように電解槽上方に配置し、電解スライムの除去と、その電解スライムを含む電解液の吸引と、濾過後電解液の供給を、電解液への浸漬と同期しながら、スクレイバー部Sを電解液に全没させる(図7(b)参照)。なお、カソードの純度を維持、向上させるためには、この電解液の供給は、濾過後電解液のみの供給に限らず、別途供給装置を準備、使用して不純物の少ない清浄な電解液(例えば、未使用の電解液など)を供給しても良い。   In that case, at least two numbered electrolytic slime recovery devices are used, and two of the electrolytic slime recovery devices are paired and arranged above the electrolytic cell so that each one is installed on both sides of the anode. The scraper part S is completely immersed in the electrolytic solution while the removal of the slime, the suction of the electrolytic solution containing the electrolytic slime, and the supply of the electrolytic solution after filtration are synchronized with the immersion in the electrolytic solution (FIG. 7B). reference). In order to maintain and improve the purity of the cathode, the supply of the electrolytic solution is not limited to the supply of only the electrolytic solution after filtration. , Unused electrolytic solution, etc.) may be supplied.

次に、図7(c)のようなクランクシャフト21を使用した運転機構を用い、奇数番目と偶数番目の電解スライム回収装置を交互動作させ、スクレイバー部S及び供給部Cを、図3に示すスクレイバー部Sの除去具5の形態に沿った動作、即ち、上下動又は横動、或いはそれらの組み合わせの動作により、アノード表面に発生する電解スライムの除去と、その電解スライムを含む電解液の吸引による回収作業を実施する。通常、電解槽底方向への動作(上下動)と、横方向への動作(横動)を組み合わせたパターンにより電解スライムの回収作業が行われる。Mはモーター、20は軸受を示す。
なお、本発明においては、この回収装置の稼働は、電解精製の稼働中でもアノード表面に発生する電解スライムを回収することが可能である。
電解スライムの除去が終了した時点で、運転を止め、回収装置を電解液内から電解槽上方に引き上げて終了する。
Next, using an operating mechanism using the crankshaft 21 as shown in FIG. 7C, the odd-numbered and even-numbered electrolytic slime recovery devices are alternately operated, and the scraper part S and the supply part C are shown in FIG. Removal of the electrolytic slime generated on the anode surface and suction of the electrolytic solution containing the electrolytic slime by the operation along the form of the removal tool 5 of the scraper part S, that is, the vertical movement or lateral movement, or a combination thereof. Carry out the collection work. Usually, the recovery operation of the electrolytic slime is performed by a pattern in which the operation toward the bottom of the electrolytic cell (up and down movement) and the operation in the horizontal direction (lateral movement) are combined. M represents a motor, and 20 represents a bearing.
In the present invention, the operation of the recovery device can recover the electrolytic slime generated on the anode surface even during the operation of electrolytic purification.
When the removal of the electrolytic slime is completed, the operation is stopped, and the recovery device is pulled up from the electrolytic solution to the upper side of the electrolytic cell, and the process is terminated.

なお、本発明に係る電解スライムの回収装置は、使用する電解槽のアノード全数に設置可能な数を準備し、一度に全数のアノード表面の電解スライムを回収しても良く、電解槽を区画化し、その区画に所属する全てのアノードから電解スライムを回収する方法を採用しても良い。
本発明に係る電解スライムの回収装置は電解中に電解スライムが増えると、アノードとカソード間の電圧が上昇するので電圧に閾値を設定し、閾値を超えた電解槽に対して上述の電解スライムを回収する方法を行うことで、高効率な操業を維持することができるようになる。
Note that the electrolytic slime recovery device according to the present invention may prepare a number that can be installed in the total number of anodes of the electrolytic cells to be used, and may collect the total number of electrolytic slimes on the anode surface at a time. A method of collecting electrolytic slime from all anodes belonging to the compartment may be adopted.
In the electrolytic slime recovery device according to the present invention, when the electrolytic slime increases during electrolysis, the voltage between the anode and the cathode rises. Therefore, a threshold is set for the voltage, and the above-mentioned electrolytic slime is applied to the electrolytic cell exceeding the threshold. By performing the recovery method, it becomes possible to maintain a highly efficient operation.

1 電解槽
2 電解液
2’ 電解液の液面
3 アノード
4 カソード
5 除去具
5a ブラシ型除去具
5b たわし型除去具
5c ヘラ型除去具
6 吸引口
7 吸引部
8 浄液フィルタ
8a 濾過ポット
9 輸送管
10 供給口
100 本発明に係る電解スライム回収装置
20 軸受
21 クランクシャフト
A 電解スライム除去部
B 電解スライム回収部
C 供給部
M モーター
送液ポンプ
S、S、S、S、Sn+1 スクレイバー部
Sa、Sc 別体型スクレイバー部
Sb、Sd 一体型スクレイバー部
b 開閉弁
h 隔壁
DESCRIPTION OF SYMBOLS 1 Electrolysis tank 2 Electrolyte 2 'Electrolyte liquid level 3 Anode 4 Cathode 5 Remover 5a Brush type remover 5b Brush type remover 5c Spatula type remover 6 Suction port 7 Suction part 8 Clean solution filter 8a Filter pot 9 Transport Pipe 10 Supply port 100 Electrolytic slime recovery apparatus 20 according to the present invention Bearing 21 Crankshaft A Electrolytic slime removal part B Electrolytic slime recovery part C Supply part M Motor P 1 Liquid feed pump S, S 1 , S 2 , Sn , S n + 1 Scraper part Sa, Sc Separate type scraper part Sb, Sd Integrated type scraper part b On-off valve h Bulkhead

Claims (10)

金属の電解精製時に、カソードと前記カソード表面と対向して配置されるアノードと、前記カソード及びアノードが浸漬している電解液を貯留した電解槽における前記アノード表面に発生する電解スライムの回収装置であって、
前記アノード表面の前記電解スライムを、前記アノード表面から除去する除去具と、
前記除去具と一体若しくは隣接して設けられ、前記電解スライムを含んだ電解液の吸引口を有する吸引部を含むスクレイバー部を、
備えることを特徴とする電解スライム回収装置。
A device for recovering electrolytic slime generated on the anode surface in an electrolytic cell storing an anode disposed opposite to the cathode and the cathode surface, and an electrolytic solution in which the cathode and anode are immersed, during electrolytic refining of metal There,
A removal tool for removing the electrolytic slime on the anode surface from the anode surface;
A scraper portion including a suction portion provided integrally or adjacent to the removal tool and having a suction port for an electrolyte solution containing the electrolytic slime,
An electrolytic slime recovery device comprising:
前記スクレイバー部が、前記除去具が配置されたアノードと対向した位置のカソードの表面に近接した位置、且つ略平行な位置に配置される隔壁を有することを特徴とする請求項1に記載の電解スライム回収装置。   2. The electrolysis according to claim 1, wherein the scraper portion has a partition wall disposed at a position close to and substantially parallel to the surface of the cathode facing the anode on which the removal tool is disposed. Slime recovery device. 前記吸引部により吸引された電解スライムを含んだ電解液から、前記電解スライムを分離して濾過後電解液を生成し、分離した前記電解スライムを回収する電解スライム回収部と、
前記濾過後電解液を、前記電解槽に循環供給する供給部を備えることを特徴とする請求項1に記載の電解スライム回収装置。
An electrolytic slime recovery unit that separates the electrolytic slime from the electrolytic solution containing the electrolytic slime sucked by the suction unit, generates an electrolytic solution after filtration, and recovers the separated electrolytic slime;
The electrolytic slime recovery apparatus according to claim 1, further comprising a supply unit that circulates and supplies the electrolytic solution after filtration to the electrolytic cell.
前記電解スライム回収部が、電解スライムを含んだ電解液から、前記電解スライムを濾し取り、回収電解スライムと濾過後電解液に分離する浄液フィルタを有することを特徴とする請求項3に記載の電解スライム回収装置。   The said electrolytic slime collection | recovery part has a liquid filter which filters the said electrolytic slime from the electrolyte solution containing electrolytic slime, and isolate | separates it into the collect | recovered electrolytic slime and the electrolyte solution after filtration, The said Claim 3 characterized by the above-mentioned. Electrolytic slime recovery device. 前記供給部が、前記除去具が配置されたアノードと対向した位置のカソードの表面に近接した位置、且つ略平行な位置に配置される隔壁とカソード間に、前記濾過後電解液を放出する供給口を有することを特徴とする請求項3又は4に記載の電解スライム回収装置。   Supply in which the supply unit releases the post-filtration electrolyte solution between a partition wall and a cathode disposed close to the surface of the cathode at a position facing the anode on which the removal tool is disposed and a position substantially parallel to the cathode The electrolytic slime recovery device according to claim 3 or 4, further comprising a mouth. 前記除去具の配置が、逆V字構造であることを特徴とする請求項1乃至5のいずれか1項に記載の電解スライム回収装置。   The electrolytic slime recovery apparatus according to any one of claims 1 to 5, wherein an arrangement of the removal tool is an inverted V-shaped structure. 請求項1乃至6のいずれか1項に記載の電解スライム回収装置を、電解槽上方に吊り下げた状態から、電解槽内における前記回収装置の設置箇所に配置する際に、前記電解槽に貯留された電解液に前記回収装置の吸引部が浸漬した時点から順次、アノード表面の電解スライムの除去処理と、アノード表面近傍の電解スライムを含む電解液の吸引と、カソード表面近傍への電解液の供給を開始することを特徴とする電解スライム回収方法。   The electrolytic slime recovery device according to any one of claims 1 to 6 is stored in the electrolytic cell when the electrolytic slime recovery device is disposed at an installation location of the recovery device in the electrolytic cell from a state suspended from the electrolytic cell. In order from the time when the suction part of the recovery device is immersed in the electrolyte solution, the removal treatment of the electrolyte slime on the anode surface, the suction of the electrolyte solution containing the electrolyte slime near the anode surface, and the electrolyte solution near the cathode surface An electrolytic slime recovery method characterized by starting supply. 少なくとも偶数基の請求項1乃至6のいずれかに記載の電解スライム回収装置を用い、
前記電解スライム回収装置をナンバリングし、
前記電解スライム回収装置の2基を対とし、アノード両面に各1基が設置されるように配置し、
前記電解スライム回収装置の除去具及び吸引口を前記電解液中に液没させながら、
前記電解スライム回収装置の前記除去具による電解スライムの除去処理と、アノード表面近傍の電解スライムを含む電解液の吸引と、カソード表面近傍への電解液の供給を、奇数番目と偶数番目の電解スライム回収装置を交互動作させてアノード表面に発生する電解スライムを含む電解液を回収することを特徴とする電解スライム回収方法。
Using the electrolytic slime recovery device according to any one of claims 1 to 6 of at least an even number group,
Numbering the electrolytic slime recovery device,
Two sets of the electrolytic slime recovery device are paired, and arranged so that each one is installed on both sides of the anode,
While immersing the removal tool and suction port of the electrolytic slime recovery device in the electrolytic solution,
Electrolytic slime removal treatment by the removal tool of the electrolytic slime recovery device, suction of an electrolytic solution containing electrolytic slime in the vicinity of the anode surface, and supply of the electrolytic solution to the vicinity of the cathode surface are performed at odd-numbered and even-numbered electrolytic slime. An electrolytic slime recovery method comprising recovering an electrolytic solution containing electrolytic slime generated on the anode surface by alternately operating a recovery device.
電解精製の稼働中に前記電解スライム回収装置を用いてアノード表面に発生する電解スライムを回収することを特徴とする請求項7又は8に記載の電解スライム回収方法。
The electrolytic slime recovery method according to claim 7 or 8, wherein the electrolytic slime generated on the anode surface is recovered using the electrolytic slime recovery device during the operation of electrolytic purification.
前記電解スライム回収装置に設置された除去具を電解槽上部に、除去具部分を下方に向けて吊り下げた状態から、前記除去具を電解槽底方向に移動させ、前記除去具が電解槽に貯留された電解液中に全没した後に、電解スライム回収装置の交互動作を開始することを特徴とする請求項7乃至9のいずれか1項に記載の電解スライム回収方法。   From the state where the removal tool installed in the electrolytic slime recovery device is hung on the top of the electrolytic cell and the removal tool part is directed downward, the removal tool is moved toward the bottom of the electrolytic cell, and the removal tool is moved to the electrolytic cell. 10. The electrolytic slime recovery method according to any one of claims 7 to 9, wherein the alternating operation of the electrolytic slime recovery device is started after being completely immersed in the stored electrolytic solution.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112695347A (en) * 2020-12-18 2021-04-23 贵阳铝镁设计研究院有限公司 Pneumatic scraping suction nozzle for aluminum
CN113215623A (en) * 2021-05-21 2021-08-06 中南大学 Automatic silt device of arranging of electrolysis trough

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS586994A (en) * 1981-06-30 1983-01-14 コミンコ・リミテツド Electrode purifying method and device
JPH0565685A (en) * 1991-09-06 1993-03-19 Toho Aen Kk Device for removing slime on anode
JP2003221692A (en) * 2002-01-31 2003-08-08 Nippon Mining & Metals Co Ltd Process for removing floating slime from electrolyte

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS586994A (en) * 1981-06-30 1983-01-14 コミンコ・リミテツド Electrode purifying method and device
JPH0565685A (en) * 1991-09-06 1993-03-19 Toho Aen Kk Device for removing slime on anode
JP2003221692A (en) * 2002-01-31 2003-08-08 Nippon Mining & Metals Co Ltd Process for removing floating slime from electrolyte

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112695347A (en) * 2020-12-18 2021-04-23 贵阳铝镁设计研究院有限公司 Pneumatic scraping suction nozzle for aluminum
CN112695347B (en) * 2020-12-18 2022-08-26 贵阳铝镁设计研究院有限公司 Pneumatic scraping suction nozzle for aluminum
CN113215623A (en) * 2021-05-21 2021-08-06 中南大学 Automatic silt device of arranging of electrolysis trough

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