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JPH09291389A - Electrolytic bath for wet copper electrolysis - Google Patents

Electrolytic bath for wet copper electrolysis

Info

Publication number
JPH09291389A
JPH09291389A JP8130766A JP13076696A JPH09291389A JP H09291389 A JPH09291389 A JP H09291389A JP 8130766 A JP8130766 A JP 8130766A JP 13076696 A JP13076696 A JP 13076696A JP H09291389 A JPH09291389 A JP H09291389A
Authority
JP
Japan
Prior art keywords
cathode
electrolytic bath
guide
cathode plate
electrolysis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8130766A
Other languages
Japanese (ja)
Inventor
Isao Yoshimura
功 吉村
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP8130766A priority Critical patent/JPH09291389A/en
Publication of JPH09291389A publication Critical patent/JPH09291389A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the bulging of the peripheral edge of a product cathode plate due to the electrolytic edge effect and to increase the number of cathode and anode plated to be loaded in one electrolytic cell by setting a guide having a fixed width on both side walls of the electrolytic bath to be used, inserting the side end of a starting sheet to be used as a cathode and conducting electrolysis. SOLUTION: A starting sheet 1 to be used as a cathode in electrolysis is arranged along a guide 4 having a U-shaped section and previously provided at least on both side walls of an electrolytic bath 3. In this case, the width of the guide 4 covers 90-110% of the thickness of the product cathode, and the height covers at least 1-3cm of the edges of side faces of the cathode. Consequently, since the bulging of the deposited copper on the peripheral edge of the product cathode plate is suppressed, the arrangement of the anode and cathode plates supposing the bulging is not needed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、湿式銅電解におい
て用いられる電解浴槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic bath used in wet copper electrolysis.

【0002】[0002]

【従来の技術】図2は従来の湿式銅電解におけるカソー
ド板とアノード板の配置を示す図であって、1はカソー
ド板、2はアノード板、3は電解液を満たした電解浴槽
である。一般的な湿式銅電解において、カソードとなる
種板1と、アノード板2とはクロスビーム4に吊り手リ
ボン5を介して交互に電解浴槽3に吊り下げられて配置
され、アノード板2の金属成分が、直流電解によりカソ
ード板1に精製、析出されるよう構成されている。
2. Description of the Related Art FIG. 2 is a view showing an arrangement of a cathode plate and an anode plate in a conventional wet copper electrolysis, wherein 1 is a cathode plate, 2 is an anode plate, and 3 is an electrolytic bath filled with an electrolytic solution. In a general wet copper electrolysis, a seed plate 1 serving as a cathode and an anode plate 2 are alternately hung from a cross beam 4 via a hanging ribbon 5 in an electrolytic bath 3 and arranged. The components are configured to be purified and deposited on the cathode plate 1 by direct current electrolysis.

【0003】[0003]

【発明が解決しようとする課題】電解の進行につれ、カ
ソード板1には精製された金属が折出するが、この際に
カソード板1の周縁部は電解のエッジ効果により、カソ
ード板の残りの部分(中央部分)より金属の析出する速
度が速くなる傾向にある。この結果、製品カソード板
1′は、図3に示すように、カソード板の周縁部が中央
部分より盛り上がった状態となり、この盛り上がり部分
は、他の中央部分よりもアノード板2と接近するので電
気的短絡を防止するため、電解浴槽3内に設置されるカ
ソード板1とアノード板2との間隔を予め広く保ってお
く必要がある。この間隔の広さは、そのまま電解浴槽3
内に設置できるカソード板1とアノード板2の装填枚数
の制限となり、1つの電解浴槽当たりの生産量を制約す
ることになる。
As the electrolysis progresses, purified metal is deposited on the cathode plate 1. At this time, the peripheral edge of the cathode plate 1 is left behind by the edge effect of electrolysis. The metal deposition rate tends to be faster than the portion (central portion). As a result, the product cathode plate 1'is in a state in which the peripheral edge of the cathode plate is raised from the central portion as shown in FIG. 3, and this raised portion is closer to the anode plate 2 than the other central portions, so that the electric In order to prevent a physical short circuit, it is necessary to keep a wide space between the cathode plate 1 and the anode plate 2 installed in the electrolytic bath 3 in advance. The width of this interval is the same as the electrolytic bath 3
This limits the number of cathode plates 1 and anode plates 2 that can be installed inside and limits the production amount per electrolytic bath.

【0004】このように湿式銅電解工程において、カソ
ード板とアノード板との間隔を決定している要因は、カ
ソード板の周縁部の盛り上がりであって、カソード板と
アノード板との間は、この盛り上がりを予め想定した間
隔にしなければならないため、単純に狭くはならないの
である。カソード板とアノード板との間隔をできるだけ
狭くし、1つの電解浴槽当たりの生産能力を高めるため
には、該盛り上がりを抑制する改善策を検討する必要が
あった。
As described above, in the wet copper electrolysis process, the factor that determines the distance between the cathode plate and the anode plate is the swelling of the peripheral portion of the cathode plate. Since the ridges must be spaced at the intervals assumed in advance, they cannot be simply narrowed. In order to make the space between the cathode plate and the anode plate as narrow as possible and to increase the production capacity per electrolytic bath, it was necessary to study an improvement measure for suppressing the swell.

【0005】そこで本発明の目的は、電解浴槽内にカソ
ード板の設置のために予めガイドを形成しておき、この
ガイドによって湿式銅電解工程で生じるカソード板の周
縁部の盛り上がりを防止すると共に、電解浴槽へのカソ
ード板の設置を容易にする湿式銅電解用の電解浴槽を提
供することである。
Therefore, an object of the present invention is to preliminarily form a guide for installing the cathode plate in the electrolytic bath, and to prevent the peripheral edge of the cathode plate from rising in the wet copper electrolysis process by the guide. An object of the present invention is to provide an electrolytic bath for wet copper electrolysis that facilitates installation of a cathode plate in the electrolytic bath.

【0006】[0006]

【課題を解決するための手段】上記問題を改善するため
には、本発明者は種々検討した結果、カソード板の周縁
部の盛り上がりを抑制するために、電解浴槽内のカソー
ド板の設置部分にガイドを設けることを見出して本発明
を完成するに至った。すなわち、本発明はカソードとな
る種板が電解浴槽の少くとも両側壁に予め設けられたガ
イドに沿って設置され、また該ガイドの幅が、電解終了
時の製品カソードの厚さの90%〜110%の範囲で、
かつ前記カソードの少くとも両側面の縁部の1cm〜3
cmの範囲を覆う湿式銅電解用の電解浴槽を特徴とする
ものである。
In order to solve the above problems, as a result of various studies by the present inventor, as a result, in order to suppress the rising of the peripheral portion of the cathode plate, the cathode plate is installed in the electrolytic bath. The present invention has been completed by finding that a guide is provided. That is, according to the present invention, a seed plate serving as a cathode is installed along a guide provided on at least both side walls of the electrolytic bath, and the width of the guide is 90% of the thickness of the product cathode at the end of electrolysis. In the range of 110%,
And 1 cm to 3 at the edge of at least both sides of the cathode
It is characterized by an electrolytic bath for wet copper electrolysis covering a range of cm.

【0007】[0007]

【発明の実施の形態】本発明者は、種々のガイド幅やガ
イドの位置において前記カソード板の盛り上がりを調査
したところ、ガイドの幅が、電解後の製品カソード板の
中央部分の厚さ90%〜110%の範囲とし、かつ前記
ガイドは、カソード板の少くとも両側面の縁部に、1c
m〜3cmの範囲の幅部分を覆うように設置すれば盛り
上がりを抑制することができることを見出だした。前記
ガイドの幅が、製品カソード板の中央部分の厚さ90%
未満とした場合、カソード板の周縁部が他の部分と比較
して薄くなりすぎ、一方製品カソード板の中央部分の厚
さの110%を超えると、該盛り上がりの抑制効果は低
下してしまう。さらに、カソードの少くとも両側面の縁
部の1cm〜3cmの範囲を覆うことにより、盛り上が
り抑制効果が十分に実現される。
BEST MODE FOR CARRYING OUT THE INVENTION The present inventor investigated the swelling of the cathode plate at various guide widths and guide positions, and found that the width of the guide was 90% of the thickness of the central portion of the product cathode plate after electrolysis. ˜110% range, and the guide is 1c at least at the edges of both sides of the cathode plate.
It has been found that the bulge can be suppressed by installing so as to cover the width portion in the range of m to 3 cm. The width of the guide is 90% of the thickness of the central portion of the product cathode plate.
If it is less than the above range, the peripheral portion of the cathode plate becomes too thin as compared with other portions. On the other hand, if it exceeds 110% of the thickness of the central portion of the product cathode plate, the effect of suppressing the swelling will decrease. Furthermore, by covering at least the range of 1 cm to 3 cm at the edges of both side surfaces of the cathode, the effect of suppressing swelling is sufficiently realized.

【0008】本発明によると、湿式銅電解工程で生じる
カソード板の周縁部の盛り上がりを十分に抑制でき、し
たがって盛り上がりを予め想定した間隔をおいてアノー
ド板とカソード板を設置する必要がない。その結果1つ
の電解浴槽当たりのカソード板、アノード板の設置枚数
を増やすことが可能となり、1つの電解浴槽当たりの生
産能力の向上が図れるのである。
According to the present invention, it is possible to sufficiently suppress the swelling of the peripheral portion of the cathode plate that occurs during the wet copper electrolysis process, and therefore it is not necessary to install the anode plate and the cathode plate at an interval which is assumed in advance. As a result, it is possible to increase the number of cathode plates and anode plates to be installed per electrolysis bath, and to improve the production capacity per electrolysis bath.

【0009】本発明を図面に基づいて説明すると、図1
に示す本発明の電解浴槽において、湿式銅電解用の電解
浴槽3にはその両側壁3′或いは該両側壁3′と底面
3″(図示せず)に亘って断面コ字状のガイド4が複数
個相互に平行に設けられており、該ガイド4は電気的絶
縁物、例えば塩化ビニール樹脂等で製作されている。そ
して、アノード板2、カソード板1が交互に電解浴槽3
内に配置されるが、このときカソード板1は、該ガイド
4に沿って挿入されて所定の位置に配置される。一方ア
ノード板2は従来と同様に吊り下げ式に支持される。こ
のように前記ガイド4により、電解浴槽3へのカソード
板1の設置が容易となり、従来技術以上に狭い間隔でア
ノード板2とカソード板1を配置できる。
Referring to the drawings, the present invention will be described with reference to FIG.
In the electrolytic bath of the present invention shown in FIG. 1, the electrolytic bath 3 for wet copper electrolysis is provided with a guide 4 having a U-shaped cross section over both side walls 3'or both side walls 3'and a bottom surface 3 "(not shown). A plurality of guides 4 are provided in parallel with each other, and the guides 4 are made of an electrically insulating material such as vinyl chloride resin, etc. Then, the anode plates 2 and the cathode plates 1 are alternately arranged.
At this time, the cathode plate 1 is inserted along the guide 4 and arranged at a predetermined position. On the other hand, the anode plate 2 is supported in a hanging manner as in the conventional case. As described above, the guide 4 facilitates the installation of the cathode plate 1 in the electrolytic bath 3, and the anode plate 2 and the cathode plate 1 can be arranged at a narrower interval than in the prior art.

【0010】そして前記ガイド4は、電解後の製品カソ
ード板の中央部分の厚さ90%〜110%の範囲の幅を
有し、かつカソード板1の少くとも両側面の縁部に、1
cm〜3cmの範囲の幅部分を覆うので、前記した通り
製品カソード板の周縁部の盛り上がりを抑制でき、電解
浴槽3内のアノード板2、カソード板1の装填枚数を増
やすことができる。
The guide 4 has a width in the range of 90% to 110% of the thickness of the central portion of the product cathode plate after electrolysis, and has a width of 1 at least at the edges of both sides of the cathode plate 1.
Since the width portion in the range of 3 cm to 3 cm is covered, the rise of the peripheral portion of the product cathode plate can be suppressed as described above, and the number of loaded anode plates 2 and cathode plates 1 in the electrolytic bath 3 can be increased.

【0011】なお、カソード板の周縁部の盛り上がりを
一層抑制するために、クロスビームにリボンを介してカ
ソード板1を接続した後、前記ガイド4と同様の形状で
同一材質のカバーをカソード板の上縁部に被着して電解
すると好ましい。
In order to further suppress the rising of the peripheral edge of the cathode plate, after connecting the cathode plate 1 to the cross beam via the ribbon, a cover made of the same material and having the same shape as the guide 4 is attached to the cathode plate. It is preferable to adhere to the upper edge and electrolyze.

【0012】[0012]

【実施例】次に、図1に基づいて本発明の実施例を説明
すると、湿式銅電解前のカソード板1の概寸法は厚さが
1mmで、幅×高さが1000mm×1000mmであ
り、かつ重さが8kgであって、一方アノード板2の概
寸法は厚さが150mmで、幅×高さが1000mm×
1000mmである。またガイド4の寸法は、幅80m
m、長さ1100mm、深さ175mmとし、260m
mの間隔をおいて電解浴槽3内の両側壁3′に設けた。
なおこれらの寸法は、製品カソード板の平均寸法から設
定された。
EXAMPLE Next, an example of the present invention will be described with reference to FIG. 1. The general dimensions of the cathode plate 1 before wet copper electrolysis are 1 mm in thickness and 1000 mm in width × 1000 mm in height, The weight of the anode plate 2 is 8 kg, and the anode plate 2 has a thickness of 150 mm and a width x height of 1000 mm x.
It is 1000 mm. The guide 4 has a width of 80 m.
m, length 1100 mm, depth 175 mm, 260 m
They were provided on both side walls 3'in the electrolytic bath 3 at intervals of m.
These dimensions were set from the average dimensions of the product cathode plate.

【0013】上記電解浴槽の採用により従来よりも狭い
間隔でアノード板とカソード板を配置できるようにな
り、寸法2600mm×1300mm×1300mmの
電解浴槽3に対するカソード板、アノード板の装填枚数
は8%増加した。
By adopting the above electrolytic bath, the anode plate and the cathode plate can be arranged at a narrower interval than before, and the number of cathode plates and anode plates loaded in the electrolytic bath 3 having a size of 2600 mm × 1300 mm × 1300 mm is increased by 8%. did.

【0014】[0014]

【発明の効果】以上述べた通り、本発明によって、湿式
銅電解時のアノード板とカソード板の銅電解浴槽内の装
填枚数を8%増加させることができ、したがって単位電
解浴槽容量当たりの生産能力を8%向上することができ
たものである。
As described above, according to the present invention, the number of anode plates and cathode plates loaded in the copper electrolytic bath during wet copper electrolysis can be increased by 8%, so that the production capacity per unit electrolytic bath capacity can be increased. Was improved by 8%.

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

【図1】本発明の湿式銅電解浴槽の概略平面図である。FIG. 1 is a schematic plan view of a wet copper electrolytic bath of the present invention.

【図2】従来の銅電解浴槽の概略図で、(a)は側面
図、(b)は正面図である。
FIG. 2 is a schematic view of a conventional copper electrolytic bath, (a) is a side view and (b) is a front view.

【図3】従来の銅電解により得られた製品カソード板の
形状説明図で、(a)は正面図、(b)は側面図であ
る。
FIG. 3 is a shape explanatory view of a product cathode plate obtained by conventional copper electrolysis, (a) is a front view and (b) is a side view.

【符号の説明】[Explanation of symbols]

1 カソード板 1′ 製品カソード板 2 アノード板 3 電解浴槽 3′ 側壁 3″ 底面 4 ガイド 1 cathode plate 1'product cathode plate 2 anode plate 3 electrolysis bath 3'side wall 3 "bottom surface 4 guide

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 カソードとなる種板が電解浴槽の少くと
も両側壁に予め設けられたガイドに沿って設置され、ま
た該ガイドの幅が、電解終了時の製品カソードの厚さの
90%〜110%の範囲で、かつ前記カソードの少くと
も両側面の縁部の1cm〜3cmの範囲を覆うことを特
徴とする湿式銅電解用の電解浴槽。
1. A seed plate serving as a cathode is installed along a guide provided in advance on at least both side walls of an electrolytic bath, and the width of the guide is 90% to 90% of the thickness of the product cathode at the end of electrolysis. An electrolytic bath for wet copper electrolysis, characterized in that it covers 110% of the cathode and covers at least 1 cm to 3 cm of the edges of both sides of the cathode.
JP8130766A 1996-04-26 1996-04-26 Electrolytic bath for wet copper electrolysis Pending JPH09291389A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8130766A JPH09291389A (en) 1996-04-26 1996-04-26 Electrolytic bath for wet copper electrolysis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8130766A JPH09291389A (en) 1996-04-26 1996-04-26 Electrolytic bath for wet copper electrolysis

Publications (1)

Publication Number Publication Date
JPH09291389A true JPH09291389A (en) 1997-11-11

Family

ID=15042155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8130766A Pending JPH09291389A (en) 1996-04-26 1996-04-26 Electrolytic bath for wet copper electrolysis

Country Status (1)

Country Link
JP (1) JPH09291389A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001053568A1 (en) * 2000-01-21 2001-07-26 Waterpower Systems Pty Ltd Improvements in electrolysis cells
CN103757665A (en) * 2014-01-17 2014-04-30 北京矿冶研究总院 Electrolytic cathode device for three-dimensional fish scale-shaped ore pulp
CN104726893A (en) * 2015-04-17 2015-06-24 绵阳市鑫科源环保科技有限公司 Low-energy-consumption horizontal copper electrolysis device and electrolysis process thereof
CN106835196A (en) * 2017-03-20 2017-06-13 铜陵有色金属集团股份有限公司金冠铜业分公司 Produce the mixing electrolysis system of tough cathode
CN107858687A (en) * 2017-12-21 2018-03-30 惠州大亚湾双益达电路板科技有限公司 A kind of PCB etching liquids device for filtering impurities

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001053568A1 (en) * 2000-01-21 2001-07-26 Waterpower Systems Pty Ltd Improvements in electrolysis cells
US6846393B2 (en) 2000-01-21 2005-01-25 Waterpower Systems Pty Ltd Electrolysis cells
CN103757665A (en) * 2014-01-17 2014-04-30 北京矿冶研究总院 Electrolytic cathode device for three-dimensional fish scale-shaped ore pulp
CN104726893A (en) * 2015-04-17 2015-06-24 绵阳市鑫科源环保科技有限公司 Low-energy-consumption horizontal copper electrolysis device and electrolysis process thereof
CN106835196A (en) * 2017-03-20 2017-06-13 铜陵有色金属集团股份有限公司金冠铜业分公司 Produce the mixing electrolysis system of tough cathode
CN106835196B (en) * 2017-03-20 2018-10-30 铜陵有色金属集团股份有限公司金冠铜业分公司 Produce the mixing electrolysis system of tough cathode
CN107858687A (en) * 2017-12-21 2018-03-30 惠州大亚湾双益达电路板科技有限公司 A kind of PCB etching liquids device for filtering impurities

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