JPS58107496A - Horizontal type electroplating installation - Google Patents

Horizontal type electroplating installation

Info

Publication number
JPS58107496A
JPS58107496A JP20512281A JP20512281A JPS58107496A JP S58107496 A JPS58107496 A JP S58107496A JP 20512281 A JP20512281 A JP 20512281A JP 20512281 A JP20512281 A JP 20512281A JP S58107496 A JPS58107496 A JP S58107496A
Authority
JP
Japan
Prior art keywords
belt
self
anode electrode
fusing
plating
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.)
Granted
Application number
JP20512281A
Other languages
Japanese (ja)
Other versions
JPS6028920B2 (en
Inventor
Hiroyuki Hakamagi
袴着 弘幸
Kazuhiro Shiino
椎野 和博
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP20512281A priority Critical patent/JPS6028920B2/en
Publication of JPS58107496A publication Critical patent/JPS58107496A/en
Publication of JPS6028920B2 publication Critical patent/JPS6028920B2/en
Expired legal-status Critical Current

Links

Abstract

PURPOSE:To uniformize the elution of a metal from the surface of an electrode, by providing a revolving endless current passing belt having a self-dissolving anode arranged thereto in a freely detachable manner to a horizontal metal strip continuous plating tank using the aforementioned anode to facilitate the replacement of the electrode. CONSTITUTION:A metal strip A is passed between self-dissolving anodes 12, 12 in a plating tank 11 to carry out plating on the surface thereof. The electrodes 12 arranged so as to leave gaps from the strip A are constituted in a state supported by the current passing belt 15 having split type mold members 120 endlessly arranged thereto so as to cross the strip A almost at right angles. The belt 15 is driven by a shaft 20 through belt wheels 16 contacted only with vicinities of both ends thereof and bevel gears 19 and receives a current by a current supply apparatus 22 while the tension thereof is adjusted by rolls 17. Plating to the end part of the strip A is prevented by an electrode shielding plate 23. Because the electrodes 12 are always moved, O2-bubbles are shaken off even if attached to the surface thereof and, therefore, they are not immobilized and elution can be made uniform.

Description

【発明の詳細な説明】 本発明は亜鉛等の金属を金属ス) IJツブの表面に連
続的に電気鍍金するための自溶性陽極電極を備え次連続
式水平型電気鍍金設備に関するものである・ との種自溶性陽極装置を備えた連続式水平型電気鍍金設
備は通常第1図に示すようK、メッキ槽(1)と、金属
ストリップ(A)を連続的にメッキ槽(1)K導入し、
メッキ後槽外に出るようKせしめるシールロール′<2
)と、メッキ槽(1)内で金属ストリップの表WiK電
気メッキするための陽極電極(3)と、陽極電極を支持
し通電せしめる通電棒(5)と、そして檜の入側KTo
って金属ストリップに負に帯電せしめるコンダクタロー
ル(6)とから構成されている。
[Detailed Description of the Invention] The present invention relates to continuous horizontal electroplating equipment equipped with a self-fusing anode electrode for continuously electroplating metals such as zinc on the surfaces of IJ tubes. Continuous horizontal electroplating equipment equipped with a self-fusing anode device usually consists of a plating tank (1) and a metal strip (A) being continuously introduced into the plating tank (1) and K, as shown in Figure 1. death,
Seal roll ′<2 to force K to come out of the tank after plating
), an anode electrode (3) for electroplating the surface WiK of the metal strip in the plating tank (1), an energizing rod (5) that supports and energizes the anode electrode, and the entrance side KTo of the Japanese cypress.
The conductor roll (6) charges the metal strip negatively.

陽極電1i (3)は、自溶性陽極電極の場合、第2図
に示すように鍍金・金属と同種の金属からなる陽極電極
部材曽を分割して、その複数個を金属ストリップの中方
向に位置するように通電棒(5)上に接触させて配設さ
れている・この場合上側の陽極電極部材(1)はその両
端肩部に取手(4)を形成して2つの通電棒(5)に懸
架して接触支持されて−る・下側の陽極電極部材は鍍金
浴中に配置した2つの通電棒(5)上に接触するように
載置して支持されている・分割量の自溶性陽極電極部材
曽は使用条件によって多少異なるが、伺えば電気亜鉛鍍
金を行う場合には、  700(長さ)X5G(巾)×
60〜100(厚み)W程度の角柱材が金属ス) IJ
ツブ巾(6OO〜2300■)K適用するように通電棒
に複数個配列して支持される・ このように構成された陽極電極は一つのメッキ槽に金属
ス) リップの走行方向に沿って鵞〜3グループ配設さ
れる。そして実用ラインでは通常このメッキ槽が直列的
に7〜10槽配設されている・ このような自溶性陽極は、電気TL鉛メッキの実用ライ
ンなどでは約1 wm/ 2 hr Ii直の消費厚み
金主じているが、溶出の不均一性などから80〜xzo
hr41C全部の自溶性陽極電極部材を交換しているの
が実情である・これらの自溶性陽極電極部材の交換作業
は、メッキ槽内での作IIが主てめるために人力による
場合が普通であp%作業のはん雑はもとよ〕、時間を長
く畳し、自溶性陽極による電気メッキを行う場合の大き
な問題点となっている一本発明の1つの目的はり前記の
ような自溶性陽極電極に用いて連続的に水平臘電gAメ
ツ*t−行う場合の問題点である\自溶性陽極電極部材
の交換作業を簡単容易に行わしめるとともに、それらI
ICIIする時間會極力短かくしうる電気メツキ設備を
提供することKToる・更に自溶性陽極電極を用いて電
気メッキを行う場合は、自溶性陽極電極表面から鍍金・
金属を均一に溶出させることが必要であるが1自溶性陽
極電極表間では01ガスの発生もとも表いそのQ、ガス
がメッキ浴中に遣轟に分散しないと自溶性陽極電極表面
に耐着したOlガスはその表面を局部的に不動態化し、
そのため自溶性陽極電極表面からの鍍金・金属am出が
阻害される・十のため鍍金浴の鍍金・金属の濃度の1I
I11が困難となp・ひいては金属ストリップへの均一
な鍍金が出来ない等の問題があり、この点を解決しよう
とすゐものである。
For the anode electrode 1i (3), in the case of a self-fusing anode electrode, as shown in Fig. 2, the anode electrode member made of the same type of metal as the plating/metal is divided, and a plurality of pieces are placed in the middle direction of the metal strip. In this case, the upper anode electrode member (1) has handles (4) formed on its shoulders at both ends, and is connected to the two current-carrying rods (5). ) The lower anode electrode member is placed in contact with and supported on two current-carrying rods (5) placed in the plating bath. The self-fusing anode electrode material size differs slightly depending on the conditions of use, but if electrolytic zinc plating is used, the size is 700 (length) x 5G (width) x
60~100 (thickness) W prismatic material is metal) IJ
A plurality of anodes are arranged and supported on a current-carrying rod so that the lip width (600~2300mm) is applied.The anode electrode configured in this way is placed in one plating tank with a metal strip along the running direction of the lip. ~3 groups will be arranged. In a practical line, 7 to 10 plating tanks are usually arranged in series. In a practical line for electric TL lead plating, such a self-fusing anode has a consumption thickness of approximately 1 wm/2 hr Ii direct. Although it mainly consists of gold, due to the non-uniformity of elution etc.
The reality is that all self-fusing anode electrode members of hr41C are replaced.The replacement work for these self-fluxing anode electrode members is usually done manually because the work is mainly done in the plating tank. One of the objects of the present invention is to solve the above-mentioned problem, which is a major problem when performing electroplating using a self-soluble anode, which takes a long time and requires a lot of time. In addition to making it easy to replace the self-fusing anode electrode member, which is a problem when continuously performing horizontal electric current using a self-fusing anode electrode,
To provide electroplating equipment that can shorten the time required for ICII as much as possible.Furthermore, when electroplating is performed using a self-fusing anode electrode, the plating process starts from the surface of the self-fusing anode electrode.
It is necessary to elute the metal uniformly, but gas is naturally generated between the surfaces of the self-fusing anode. The deposited Ol gas locally passivates the surface,
Therefore, plating/metal am release from the surface of the self-fusing anode electrode is inhibited.
There is a problem that I11 is difficult to coat and evenly it is not possible to uniformly plate the metal strip, and this is an attempt to solve this problem.

本発明のl!に他の目的は、電気メッキ[11して、I
I溶性陽極電□極の表面から鍍金・金属が均一に溶出す
ることの出来る電気メツキ設備を提供することにある。
l of the present invention! Other purposes include electroplating [11 and I
An object of the present invention is to provide electroplating equipment that can uniformly elute plating and metal from the surface of an I-soluble anode electrode.

本発明は上述のような問題を解決するためになされ7t
ものであり、メッキ槽を通過する金属ストリップに所定
間隔をおいてほぼ直交するようにエンドレスに配置され
た陽極電極支持用通電ベルトと、該ベルト上圧着脱自在
に取り付けた分割型自溶性陽極電極部材と、該ベル)を
支持し1回動せしめる一対のベルト車と、該ベルト車を
駆動する駆動機構と、該ベルトへlDW!触型導電型導
電装置ッキ槽に付設してなることを基本的な特徴とする
鴨のである・ 以下この発明を図面の実施例によって説明する。
The present invention has been made to solve the above-mentioned problems.
It consists of an energizing belt for supporting the anode electrode arranged endlessly at predetermined intervals and almost orthogonal to the metal strip passing through the plating bath, and a split self-fusing anode electrode detachably attached to the belt by pressure. member, a pair of belt pulleys that support and move the belt once, a drive mechanism that drives the belt pulley, and an IDW! The present invention will be described below with reference to the embodiments shown in the drawings.

この発明を適用した水平型電気メツキ設備は、第3図の
歓略@面図に示されるようK。
The horizontal electroplating equipment to which this invention is applied is shown in the schematic diagram of FIG.

メッキ檜U内にある2つの自溶性陽極電極(ロ)(ロ)
の間を金属ストリップ囚が通過することによって金属ス
トリップ囚の表面Kff金が行われるようになっている
。メッキ槽Q車の金属ストリップ囚の進行方向両港には
、金属ストリップを通過せしめる各々一対のシールロー
ル(2)が設けられている。又金属ストリップへの負の
帯電を行うためにメッキ槽α薯の入11にはコンダクタ
ロールa4が設けられている。この発明の自溶性陽極電
極は、第3図、第4@tic示されるように、金属スト
リップ囚に間隔をおいて配置された自溶性陽極電極(6
)はそれを構成する分割型自溶性陽極電極部材(120
)がエンドレスの通電用ベルト(2)上に接触支持され
ている。エンドレス通電ベルト(ト)を回動せしめる一
対のベルト車(ロ)は、皺ベルトの両端近傍とのみ接触
するようKL7を軍縮型のベルト車となっている・これ
は通電ベルト内側Km着した自溶性陽極電極部材(ig
o)がベルト車(ロ)を通過する時に接触しないように
したものである。ベルト車(ロ)は通電ベルト(6)の
両端近傍とのみ接触し、自溶性陽極電極部材(120)
とベルト車(至)との軸傾とは所定の隙間を構成してい
る・ベルト車(ロ)は両端に設けたカサ歯車(ロ)を介
してメッキ槽の上方から画工する駆動軸(ホ)と連結し
ている◎通電ベルト(ロ)への通電はカーボンブラシの
ような接触層導電装置@によって回動する通電ベルト(
ロ)K連続的に通電される。第3図においてはベルトの
両端近傍で行ってい石、なお、図中0ηは通電ベルトの
張力調整ロールてあり、昇降可能となっている。1+■
は軸受け、に)は金属ストリップの端部への過メッキを
防止するための電極じゃへい板である。
Two self-fusing anode electrodes inside the plated cypress U (b) (b)
The surface of the metal strip is coated by passing the metal strip between the two. A pair of seal rolls (2) for allowing the metal strip to pass are provided at both ports of the plating tank Q vehicle in the direction of movement of the metal strip. Further, a conductor roll a4 is provided in the plating bath 11 for negatively charging the metal strip. The self-fusing anode electrode of the present invention has self-fusing anode electrodes (6
) is a split type self-fusing anode electrode member (120
) is supported in contact with an endless current-carrying belt (2). The pair of belt wheels (b) that rotate the endless energizing belt (g) are a disarmament version of KL7 so that they contact only the vicinity of both ends of the wrinkled belt. Soluble anode electrode member (ig
This prevents o) from coming into contact with the belt pulley (b) when it passes. The belt wheel (b) contacts only the vicinity of both ends of the energizing belt (6), and the self-fusing anode electrode member (120)
The axial inclination between the belt wheel and the belt wheel (to) constitutes a predetermined gap.The belt wheel (b) is connected to the drive shaft (hoto) that is applied from above the plating tank via bevel gears (b) provided at both ends. ) is connected to the ◎ current carrying belt (b), which is connected to the current carrying belt (b) which is rotated by a contact layer conducting device such as a carbon brush.
b) K is energized continuously. In FIG. 3, there are rollers near both ends of the belt, and 0η in the figure is a tension adjustment roll for the energized belt, which can be raised and lowered. 1+■
is a bearing, and 2) is an electrode shield plate to prevent over-plating on the end of the metal strip.

通電ベルトへの自溶性陽極電極部材(120)の着脱及
びその形状の一実施例を第5図、第6図、第7図に示す
、第5図は金属ストリップに間隔をおいてほぼ直交する
ように配置したエンドレス通電ベル) (IIの1区間
を示す詳細図である ここにおいてはエンドレスA電ベ
ルト(ロ)の巾中央部にベルトの長平方向く沿って強度
を失わない程度に間隔をおいて、開口る貫通孔■を設け
ている。第6図は通電ベルトと自溶性陽極電極部材(1
20)との装置の1例を示す拡大詳細図である。第7図
は自溶性陽極電極部材(120)の1例を示す斜視図で
ある。
An example of attaching and detaching the self-fusing anode electrode member (120) to and from the current-carrying belt and its shape is shown in FIGS. 5, 6, and 7. FIG. (This is a detailed view showing one section of II. A through hole (■) is provided to open the energizing belt and the self-fusing anode electrode member (1).
20) is an enlarged detailed view showing an example of the device. FIG. 7 is a perspective view showing an example of a self-fusing anode electrode member (120).

ベルトの開口部(至)Kは第6図、第7図に示すような
形状の分割型自溶性陽極電極部材(120)を装着する
。この場合、自溶性陽極電極部材(120)は通電ベル
ト(ロ)の開口S(ハ)の横の長さWよりも分割型自溶
性陽極電極部材(120)の長さ色)を長くし、その両
端の肩部は通電ベルト(至)の開口部内縁と嵌合せしめ
る溝部(ホ)を設けている。しかして自溶性陽極電極部
材の装着又は取りはずしはこの開口部(財)をとうして
人力・又は治具等を用いて簡単に行うことができる。
A split type self-fusing anode electrode member (120) having a shape as shown in FIGS. 6 and 7 is attached to the opening (to) K of the belt. In this case, the self-fusing anode electrode member (120) has the length (color) of the split type self-fusing anode electrode member (120) longer than the horizontal length W of the opening S (c) of the current-carrying belt (b); The shoulders at both ends are provided with grooves (E) that fit into the inner edges of the opening of the current-carrying belt (E). Therefore, the self-soluble anode electrode member can be easily attached or detached through this opening by hand or using a jig or the like.

次に本発明による電気メツキ設備を用いて電気メッキを
行つ逢場合につき、具体例を述べる・ 電極部材は第5図、第6図、第7図に示すようなものを
用いたー通電ベルトは巾700■1厚み約10m+のT
14合金板を用い次、自溶性陽極電極部材は500X5
0X30 (厚み)mのもので、七の上部両ylIAl
lには上乗せして肩部として高さが23mで13(巾)
X20(夷行き)■(夷行きのR−8)の溝部を形成し
た。これはメッキ金属を鋳型に鋳込んで製造した。
Next, we will describe a specific example of electroplating using the electroplating equipment according to the present invention. The electrode members shown in FIGS. 5, 6, and 7 were used as an energizing belt. Width 700 x 1 thickness approx. 10 m + T
14 alloy plate was used, and the self-fusing anode electrode member was 500X5.
0x30 (thickness) m, upper both ylIA1
The height is 23m and the width is 13 (width) by adding it to the shoulder part.
A groove portion of X20 (bound for Yoshi) and ■ (R-8 bound for Yoshi) was formed. It was manufactured by casting plated metal into a mold.

この場合の電極重量は5〜6 b1本でToシ、人力に
よって通電ベルトを少しずつ回転しながら上部側の高い
位置で順次装着を行った・電気メッキVCToたっては
陽極電極として、60 A/dm”として電解を行ない
、その間通電ベルトをゆっくりと連続的に回動させた。
In this case, the weight of the electrode was 5 to 6 lb. One electrode was installed manually at a high position on the upper side while rotating the energizing belt little by little. ・The electroplated VCTo was used as an anode electrode at 60 A/dm. Electrolysis was carried out as follows, during which the energizing belt was rotated slowly and continuously.

陽極電極部材は50禦巾のものを複数個配設したことK
よりベルト車を通過する場合も力が〃・からす円滑に回
動出来食、陽極電極は自溶性陽極電極部材の消耗が25
′¥S厚さまで行い、5蝙残部として廃却した・ それ以上の使用においては、通電ベルトとの接触が自溶
性陽極電極部材の自重を主として利用しているので、あ
まプ薄くなるとメッキ浴の液流などに左右されてその接
触の低下f:まねくことになる。
A plurality of anode electrode members with a width of 50 mm are provided.
Even when passing through the belt wheel, the force can be rotated smoothly, and the anode electrode is self-fusing.
The coating was carried out to a thickness of S and was discarded as a remaining part of the plating bath. When used beyond that, the contact with the current-carrying belt mainly utilizes the weight of the self-fusing anode electrode member, so when the plating bath becomes thinner, the plating bath becomes thinner. This will lead to a decrease in contact depending on the liquid flow, etc.

その後に自溶性陽極電極の交換を人力によって行ったが
、1本嶺りの重量が軽く取り扱いが容易であり、その取
シはすし装着は人がたった位置で行うことが出来、非常
に作業がしやすいこともあって、1槽当9の交換時間が
従来の1/6〜1/10hr K短縮することが出来た
。又、自溶性陽極電極部材は金属ス) IJツブの上l
I、下側によってその形状を変える必l!がないため在
庫の量も少なくて済み合理的であった・ 又、本発WAにおいてはベルトの回動によって陽極電極
は絶えず動いていることから陽極電極の表面にO,ガス
の気泡がついていたとしても金属ストリップの対極とし
てはずれベルト車をtわ石ところでは、骸気泡はほぼき
れいにはらい落されるので不動態化になることがなく、
その溶出も均一に行うことが出来る。
After that, the self-soluble anode electrode was replaced manually, but since the weight of a single ridge is light and easy to handle, the removal and installation can be done by a person alone, making the work extremely labor-intensive. Because it is easy to replace, the replacement time per tank was reduced by 1/6 to 1/10 hr compared to the conventional method. Also, the self-fusing anode electrode member is made of metal) above the IJ tube.
I, it is necessary to change its shape depending on the bottom side! In addition, in this WA, the anode electrode was constantly moving due to the rotation of the belt, so there were O and gas bubbles on the surface of the anode electrode. However, if a belt wheel is used as the opposite electrode of the metal strip, the bubbles will be removed almost completely, so they will not become passivated.
Its elution can also be performed uniformly.

そのため従来0自溶性陽極電極部材が、概略30〜40
箇を残して廃却されたのに対して、約5mgの残ヤでよ
く、そのため効率良く自溶性陽極電極の厚さもめまり厚
くしなくてもよい。これはとりもなおさず、取り扱−の
容品さへの起因となっている。なお、上記では電気亜鉛
メッキ會主体として説明したが、これは亜鉛のみにかぎ
らずSnなど自溶性陽極電極を用い4Iことの出来るも
のについては同様に適用出来ることは云うまでもない。
Therefore, the conventional 0 self-fusing anode electrode member was approximately 30 to 40
In contrast to the case where only a portion was discarded, only about 5 mg of residual material is required, and therefore, the thickness of the self-fusing anode electrode does not need to be increased in an efficient manner. This is a cause of poor handling. It should be noted that although the above description has been made mainly of electrogalvanizing, it goes without saying that this is applicable not only to zinc but also to other materials that can be coated with 4I using a self-fusing anode electrode such as Sn.

本発明では1通電ベルトの内側に陽極電極部材を装着し
た場合について述べたが1通電ベルトの外側に陽極電極
を装着して、通電ベルトの外側を金属ストリップを走行
させることも可能でめり、この場合は片面電気メッキな
どに適用出来るものである・ 又1通電ベルトの自溶性陽極電極部材の装着については
上述の方法に限定されるものではなく、簡単な固着を行
ってもよいが、上述のような単なる物理的な装着が出来
る場合がより実用的である。
In the present invention, the case has been described in which the anode electrode member is mounted on the inside of one energizing belt, but it is also possible to mount the anode electrode on the outside of one energizing belt and run a metal strip on the outside of the energizing belt. In this case, it can be applied to single-sided electroplating.In addition, the attachment of the self-fusing anode electrode member of the current-carrying belt is not limited to the method described above, and simple fixing may be used, but the method described above It is more practical if it can be simply physically attached.

以上のようVこ、不発明は水平式電気メツキ設備におい
て自溶性**tmt−用いて金属ストリップの表面への
電気メッキを行う場合の大きな問題点であった。収電極
部材の交換を1通電ベルトへ簡単に装着又は取りはずし
か出来るようにし、時間の短縮を大巾にはかるとともに
自溶性陽極電極表面の局部的に発生する不動態化を未然
にふせぎ、メッキ金属の溶出を均一に行わしめ、かつ自
溶性陽極電極部材を有効に消耗使用させることが出来る
等の優:n7j効果がある。
As described above, this problem was a major problem when electroplating the surface of a metal strip using self-fusing **tmt in horizontal electroplating equipment. By making it possible to easily replace the collecting electrode member by attaching it to or removing it from the current-carrying belt, this greatly reduces time and prevents localized passivation on the surface of the self-fusing anode electrode. It has excellent n7j effects such as uniform elution and effective use of the self-soluble anode electrode member.

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

第1図は従来の水平型電気鍍金設備の概略@Ilfrm
WJ、 萬2図ハ第1 図にオケ& X −X線断面図
、第3図は本発明の一実施9Ilt示す側断面図、第4
図は第3図におけるY−X線断面図、第5図は電極部材
と通電ベルトの構成の一実施例を示す斜視図、第6図は
その側面図、第7図は電極部材の斜視図である。 Qト・・メッキ槽、(ロ)・・・自溶性陽極電極、(L
l・・:シールロール、αΦ・・・コンfりfiロール
、(9)・・・通電ベルト、に)・・・ベルト車、(ロ
)・・・張力調整ロール、(至)・・・軸、(6)・・
・カサ歯車、(ホ)・・・駆動軸、(ハ)・・・軸受、
(2)・・・導電装置、OI・・・電極じゃへい板、(
財)・・・開口部、曽・・・貫通孔、(2)・・・溝部
。 %ト出纏入  日本鋼管株式会社 発 明  者   袴   着   弘   幸−椎 
  野   和   博 代理人ガ理士   吉   鳳   省   玉量  
 同      西   野    茂   美同  
弁論土   吉   鳳   弘   子第6図 第7図
Figure 1 is a schematic diagram of conventional horizontal electroplating equipment @Ilfrm
WJ, 萬 2 Figure 1 is a cross-sectional view taken along the lines X--X, Figure 3 is a side sectional view showing one embodiment of the present invention, and Figure 4 is a side sectional view showing one embodiment of the present invention.
The figure is a sectional view taken along the Y-X line in FIG. 3, FIG. 5 is a perspective view showing an example of the structure of the electrode member and the current-carrying belt, FIG. 6 is a side view thereof, and FIG. 7 is a perspective view of the electrode member. It is. Q... Plating tank, (B)... Self-fusing anode electrode, (L
l...: seal roll, αΦ...confi roll, (9)... energizing belt, ni)... belt wheel, (b)... tension adjustment roll, (to)... Axis, (6)...
・Bevel gear, (E)...Drive shaft, (C)...Bearing,
(2)... Conductive device, OI... Electrode breaker plate, (
property)...Opening, (2)...Through hole, (2)...Groove. Nippon Kokan Co., Ltd. Inventor Hakama wearing Hiroyuki Shii
Hiroshi No Kazuhiro Attorney and Physician Yoshi Otori Masaaki
Shigeru Nishino Mito
Speech by Yoshi Otori Hiroko Figure 6 Figure 7

Claims (1)

【特許請求の範囲】[Claims] メッキ槽を走行する金属ストリップに所定間隔をお2い
て、はは直交するエンドレスに配置した陽極電極支持用
通電ベルトと、腋ベルトを支持し、回転せしめる一対の
ベルト車と、該ベルト車を駆動する駆動機構と、該ベル
)O接触製導電装置とをメッキ槽に付設したことを特徴
とする水平型電気鍍金設備。
An energized belt for supporting the anode electrode is arranged endlessly at a predetermined interval and perpendicular to the metal strip running in the plating tank, a pair of belt wheels supporting and rotating the armpit belt, and a pair of belt wheels for driving the belt wheel. 1. A horizontal electroplating equipment, characterized in that a drive mechanism and a conductive device made of Bell O contact are attached to a plating tank.
JP20512281A 1981-12-21 1981-12-21 Horizontal electroplating equipment Expired JPS6028920B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20512281A JPS6028920B2 (en) 1981-12-21 1981-12-21 Horizontal electroplating equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20512281A JPS6028920B2 (en) 1981-12-21 1981-12-21 Horizontal electroplating equipment

Publications (2)

Publication Number Publication Date
JPS58107496A true JPS58107496A (en) 1983-06-27
JPS6028920B2 JPS6028920B2 (en) 1985-07-08

Family

ID=16501781

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20512281A Expired JPS6028920B2 (en) 1981-12-21 1981-12-21 Horizontal electroplating equipment

Country Status (1)

Country Link
JP (1) JPS6028920B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6174417B1 (en) 1998-05-20 2001-01-16 Process Automation International Ltd. Electroplating machine
US6261425B1 (en) 1998-08-28 2001-07-17 Process Automation International, Ltd. Electroplating machine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6174417B1 (en) 1998-05-20 2001-01-16 Process Automation International Ltd. Electroplating machine
US6241860B1 (en) 1998-05-20 2001-06-05 Process Automation International, Ltd. Electroplating machine
US6251234B1 (en) 1998-05-20 2001-06-26 Process Automation International, Ltd. Electroplating machine
US6261425B1 (en) 1998-08-28 2001-07-17 Process Automation International, Ltd. Electroplating machine

Also Published As

Publication number Publication date
JPS6028920B2 (en) 1985-07-08

Similar Documents

Publication Publication Date Title
US4367125A (en) Apparatus and method for plating metallic strip
JPH03207892A (en) Device and method for electrolytic covering of strip
US5441627A (en) Metal foil manufacturing method and an anodized film forming apparatus used therefor
JPS6238436B2 (en)
JPS58107496A (en) Horizontal type electroplating installation
US4220504A (en) Selective electroplating
EP0257670B1 (en) Process and apparatus for the deposition of bearing alloys
US2075331A (en) Method and apparatus for the electrodeposition of metal
US3691026A (en) Process for a continuous selective electroplating of strip
UA54438C2 (en) A METHOD AND AN INSTALLATION FOR ELECTROLYTIC COATING WITH A METAL LAYER ON THE SURFACE OF A CYLINDER for the continuous casting of thin metal strips
US3629077A (en) Process for plating of stripes on longitudinal electrically conductive material
DE3891150C1 (en)
JP2659910B2 (en) Apparatus for forming anodized film on cathode body surface
US4176015A (en) Method for chromium electroplating of bars
CA1165271A (en) Apparatus and method for plating one or both sides of metallic strip
JPH06146066A (en) Continuous electrolytic processor
JP2551092B2 (en) Method and apparatus for preventing over-plating of end portions of metal strip in electric plating line
JP4797635B2 (en) Tin-plated steel strip manufacturing method and tin-plating cell
JPS61139658A (en) Method for removing deposit on surface of roll in molten metallic bath for hot dipping
US5069762A (en) Appartaus for improved current transfer in radial cell electroplating
JP3361203B2 (en) Soluble anode for electroplating equipment
JPS633035B2 (en)
JPS61119698A (en) Electricity conducting roll for electroplating
JPS63293200A (en) Electroplating method
JP3122604B2 (en) Electrolytic treatment equipment