JPS63161197A - Apparatus for electrolytically treating stainless band steel - Google Patents

Apparatus for electrolytically treating stainless band steel

Info

Publication number
JPS63161197A
JPS63161197A JP30553186A JP30553186A JPS63161197A JP S63161197 A JPS63161197 A JP S63161197A JP 30553186 A JP30553186 A JP 30553186A JP 30553186 A JP30553186 A JP 30553186A JP S63161197 A JPS63161197 A JP S63161197A
Authority
JP
Japan
Prior art keywords
stainless steel
steel strip
band steel
electrodes
electrolytic
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
JP30553186A
Other languages
Japanese (ja)
Inventor
Kenichi Yanagi
謙一 柳
Shoichi Hashimoto
正一 橋本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP30553186A priority Critical patent/JPS63161197A/en
Publication of JPS63161197A publication Critical patent/JPS63161197A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To reduce the resistance of an electrolytic soln. and to save electric power by electrolytically pickling stainless band steel between negative and positive electrodes in the former stage in a horizontal electrolytic cell and with electric current supplied to the band steel through an electrode roll in the latter stage. CONSTITUTION:Stainless band steel 3 is immersed and traveled in concd. sulfuric acid as an electrolytic soln. 2 in a horizontal electrolytic cell 1. Plural pairs of electrodes 4, 5, 9, 8 are arranged above and below the band steel 3 in the inlet side former stage A in the longitudinal direction of the band steel 3 so that each pair of electrodes having opposite polarities confront each other. Plural pairs of negative electrodes 11 are arranged above and below the band steel 3 in the outlet side latter stage B so that each pair of negative electrodes confront each other. An electrode roll 13 having positive polarity and guiding the band steel 3 is placed on the outside of the outlet of the cell 1.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は熱処理したステンレス帯鋼表面のスケールを除
去する電解処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an electrolytic treatment apparatus for removing scale from the surface of a heat-treated stainless steel strip.

〈従来の技術〉 低酸素雰囲気炉による熱処理によって形成されたステン
レス帯鋼表面のスケール除去は、通常、濃硫酸電解酸洗
処理によって行われる。
<Prior Art> Removal of scale from the surface of a stainless steel strip formed by heat treatment in a low-oxygen atmosphere furnace is usually performed by electrolytic pickling treatment with concentrated sulfuric acid.

そして電解酸洗処理の前段階では、陽極、陰極どちらの
電極による電解処理においてもスケール除去が可能であ
るが、後段階では陽電i(帯鋼表面は陰極)で電解する
と蹟金効果等により表面性状が悪くなる故、必ず陰電極
(帯鋼表面は陽極)を用いる必要がある。
In the pre-electrolytic pickling process, it is possible to remove scale by electrolytic treatment using either an anode or a cathode, but in the latter stage, electrolysis with a positive electrode (the surface of the steel strip is the cathode) will cause the surface to be removed due to the pickling effect, etc. Since the properties deteriorate, it is necessary to use a negative electrode (the surface of the steel strip is an anode).

第2図は上述した要求を充たす装置の電解酸洗処理装置
の要部縦断面図であって、1は横型の電解槽で、濃硫酸
の電解液2が入れられている。そして、この電解液2に
浸漬させた入側ロール7a、出側ロール7bが回転自在
に装設されている。4および8は、電解槽1内の入側A
を走行する。ステンレス帯y43の両面にそれぞれ対設
された陽電極、5および9は出側Bを走行するステンレ
ス帯fi3の両面にそれぞれ対設された陰Ti極で、各
々の電R6および10にそれぞれ連結されている。
FIG. 2 is a longitudinal cross-sectional view of a main part of an electrolytic pickling treatment apparatus that satisfies the above-mentioned requirements, and 1 is a horizontal electrolytic cell in which an electrolytic solution 2 of concentrated sulfuric acid is placed. An inlet roll 7a and an outlet roll 7b immersed in the electrolytic solution 2 are rotatably installed. 4 and 8 are entry side A in the electrolytic cell 1
run. Positive electrodes 5 and 9 are respectively provided oppositely on both sides of the stainless steel band y43, and cathode Ti electrodes 5 and 9 are respectively provided oppositely on both sides of the stainless steel band fi3 running on the exit side B, and are connected to the respective electrodes R6 and 10. ing.

ステンレス帯鋼3は図中左側から電解博1へ入り、入側
ロール7aで案内されて電解液2中の入側Aの各陽電極
4,8及び出側Bの各陰電極5,9の間を通板し、その
間に両面を電解酸洗処理され、出側ロール7bに案内さ
れて電解槽1から出て、次の工程へ送られる。
The stainless steel strip 3 enters the electrolytic solution 1 from the left side in the figure, and is guided by the inlet roll 7a to form the positive electrodes 4 and 8 on the inlet side A and the negative electrodes 5 and 9 on the outlet side B in the electrolytic solution 2. During this time, both surfaces are subjected to electrolytic pickling treatment, and then guided by the exit roll 7b to exit the electrolytic cell 1 and sent to the next step.

〈発明が解決しようとする問題点〉 ところで、上述した電解処理は■ステンレス帯鋼の表面
性状を良好にするためには、ある一定の電流密度と電解
時間が必要である。
<Problems to be Solved by the Invention> By the way, the above-mentioned electrolytic treatment requires a certain current density and electrolysis time in order to improve the surface quality of the stainless steel strip.

そのため、帯鋼のライン速度を一定にするため、ある程
度の電極長さ、電極数が必要となり、電解液中の帯鋼長
さ、すなわち電解槽内の入側ロールと出側ロールとの間
隔が長くなり、横型の電解槽では、この各ローラで案内
されるステンレス帯鋼のたわみが大きくなるから、対向
する電極間の距離が大きくなっている。このようにステ
ンレス帯鋼の上下両面と、上下面に対向する各組電極間
距離が大きくなると、電解液抵抗が太き(なる。また、
電解液中の帯鋼長さが長いので、その入側(前段の陽電
極と対向する部位)から出側(後段の陰電極と対向する
部位)までの帯鋼抵抗も大きくなる。
Therefore, in order to keep the line speed of the strip constant, a certain length and number of electrodes are required, and the length of the strip in the electrolyte, that is, the distance between the inlet roll and the outlet roll in the electrolytic cell, is In a horizontal electrolytic cell, the deflection of the stainless steel strip guided by each roller becomes large, so the distance between the opposing electrodes becomes large. In this way, as the distance between the upper and lower surfaces of the stainless steel strip and each set of electrodes facing the upper and lower surfaces increases, the electrolyte resistance increases.
Since the length of the steel strip in the electrolytic solution is long, the resistance of the strip from the inlet side (the part facing the positive electrode in the previous stage) to the outlet side (the part facing the negative electrode in the latter stage) also becomes large.

◎さらに、同じステンレス帯鋼に複数の回路電流(第2
図の例では陽電極4から陰電極5への電流と、陽電極8
から陰電極9への電流)が流れるため、みかけの帯鋼抵
抗はその回路の数だけさらに太き(なり、大きな電源電
圧、電力が必要となる。
◎Furthermore, multiple circuit currents (secondary
In the example shown, the current flows from the positive electrode 4 to the negative electrode 5, and the current flows from the positive electrode 8 to the negative electrode 5.
Since current flows from the negative electrode 9 to the negative electrode 9, the apparent resistance of the steel strip becomes thicker by the number of circuits, and a larger power supply voltage and power are required.

そこで本発明は上述した従来のステンレス帯鋼の電解処
理装置の欠点を除去するためになされたものであって、
対向する反対極性のfS極間距離が短か(、シたがって
帯鋼抵抗が小さいのみならず、電解te低抵抗小さくか
つ複数の各′:4極間に回路電流が生じないステンレス
帯鋼の電解処理装置を提供しようとするものである。
Therefore, the present invention has been made in order to eliminate the drawbacks of the conventional electrolytic treatment equipment for stainless steel strips mentioned above.
Is the distance between the opposing fS poles of opposite polarity short?(Thus, not only the strip resistance is small, but also the electrolytic resistance is small and the stainless steel strip has a small number of electrodes. No circuit current occurs between the four poles.) The present invention aims to provide an electrolytic treatment device.

く問題点を解決するための手段〉 上述の目的を達成するため、本発明にかかるステンレス
帯鋼の電解処理装置は、横型電解槽に入れた濃硫酸電解
液中に浸漬されて走行するステンレス帯鋼の入側上下面
にそれぞれ対向して配設された互いに反対極性の対の′
ls極を複数組、当該ステンレス帯鋼の長さ方向に治っ
て順次配設する一方、ステンレス帯鋼の出側上下面にそ
れぞれ、陰電極を対にして対向配設すると共に、横型電
解槽の出側外部に、ステンレス帯鋼を誘導する陽極性の
電極ロールを設けたことを特徴とするものである。
Means for Solving the Problems> In order to achieve the above-mentioned object, the stainless steel strip electrolytic treatment apparatus according to the present invention includes a stainless steel strip that runs while being immersed in a concentrated sulfuric acid electrolyte in a horizontal electrolytic tank. Pairs of opposite polarity arranged oppositely on the upper and lower surfaces of the steel entry side, respectively.
A plurality of pairs of ls electrodes are sequentially arranged in the length direction of the stainless steel strip, while pairs of negative electrodes are arranged facing each other on the upper and lower surfaces of the outlet side of the stainless steel strip, and It is characterized in that an anodic electrode roll for guiding the stainless steel strip is provided on the outside of the exit side.

く作   用〉 以上のような構成になっているから、極性が異なるよう
に配置された入側の陽陰電極間に電流を流してステンレ
ス帯鋼前段階での電解酸洗処理では、ステンレス帯鋼の
電気抵抗を小さくできる。また、出側では電極ロールを
介してステンレス帯鋼へ通電して陽電極とし、陰電極と
の間に電流を流して該ステンレス帯鋼後段階の電解酸洗
処理を行うことができる。
Due to the above structure, in electrolytic pickling treatment in the pre-stage of stainless steel strip, the stainless steel strip is The electrical resistance of steel can be reduced. Further, on the output side, electricity is applied to the stainless steel strip through an electrode roll to serve as a positive electrode, and a current is passed between the stainless steel strip and the negative electrode to perform a post-electrolytic pickling treatment on the stainless steel strip.

く実 施 例〉 つぎに、図面に基づいて本発明の代表的な一実施例につ
いて説明する。ただし、実施例のステンレス帯鋼の電解
装置の要部構成を示す第1図中従来装置(第2図)と同
一部材には同一符号を付し、重複説明を省略することと
する。
Embodiment Next, a typical embodiment of the present invention will be described based on the drawings. However, in FIG. 1, which shows the main structure of the stainless steel strip electrolyzer of the embodiment, the same members as in the conventional device (FIG. 2) are designated by the same reference numerals, and redundant explanation will be omitted.

すなわち、第1図中、4,8は陽電極、5および9は陰
電極であり、電解槽1内の入側Aを走行するステンレス
帯@3の両面にその極性が異なるように陽陰交互に対設
され、各々の電源6,10にそれぞれ連結されている。
That is, in FIG. 1, 4 and 8 are positive electrodes, and 5 and 9 are negative electrodes, and positive and negative electrodes are alternately arranged on both sides of the stainless steel band @ 3 running on the entrance side A of the electrolytic cell 1 so that the polarities are different. and are connected to respective power sources 6 and 10, respectively.

11は、帯鋼後段電解処理用の陰電極で、電解槽1内の
出側Bを走行するステンレス帯鋼3の両面2箇所にそれ
ぞれ対設されている。
Reference numeral 11 denotes negative electrodes for the latter-stage electrolytic treatment of the steel strip, which are provided opposite to each other at two locations on both sides of the stainless steel strip 3 running on the exit side B of the electrolytic cell 1.

13は陽極性のフンダクタロールで、電解槽1の出側B
外部に回転自在に装設され、押えロール14とでステン
レス帯鋼3を挟持している。そして、陰電極11とコン
ダクタロール13とは、電源12に連結されている。1
5は一対のリンガロールで m解液2の液面とコンダク
タロール13との間のステンレス帯鋼3を所定の面圧で
挾持するように、回転自在に装設されている。
13 is a positive fundactor roll, which is located on the outlet side B of the electrolytic cell 1.
It is rotatably installed externally, and holds the stainless steel strip 3 between the presser roll 14 and the presser roll 14 . The negative electrode 11 and the conductor roll 13 are connected to a power source 12. 1
Reference numeral 5 denotes a pair of Ringer rolls, which are rotatably installed so as to sandwich the stainless steel strip 3 between the surface of the decomposition solution 2 and the conductor roll 13 with a predetermined surface pressure.

ステンレス帯鋼3は図中左側から電解槽1へ入り、入側
Aの陽電極4と陰電極5との間を通板する際に、その両
面は前段の電解酸洗処理をなされ、さらに出側Bでは、
電源12からコンダクタロール13を介して陽電流を通
電されて陽極となり、各々の陰電極11の間を通板して
電解酸洗処理を完了する。そして、電解液2から出て付
着している電解液2をリンガロール15で拭い取り、コ
ンダクタロール13と押えロール14との間を通って次
工程へ送られる。このとき、入側Aでは各々極性の異な
る陽陰電極4,5及び8,9間にのみ電流が流れ、これ
らの電気抵抗はほぼ電解液2の抵抗のみとなって、ステ
ンレス帯鋼3の抵抗はほとんど無視できる。
The stainless steel strip 3 enters the electrolytic cell 1 from the left side in the figure, and when passing between the anode 4 and the cathode 5 on the inlet side A, both sides are subjected to the electrolytic pickling treatment in the previous stage, and then the stainless steel strip 3 is subjected to the electrolytic pickling treatment in the previous stage. On side B,
A positive current is applied from the power source 12 through the conductor roll 13 to form an anode, and the plate is passed between each cathode 11 to complete the electrolytic pickling process. Then, the electrolytic solution 2 that has come out and adhered to the electrolytic solution 2 is wiped off with a ringer roll 15, and passed between the conductor roll 13 and the presser roll 14 to be sent to the next process. At this time, current flows only between the anode and cathode electrodes 4, 5 and 8, 9 having different polarities on the inlet side A, and their electrical resistance is almost only the resistance of the electrolyte 2, and the resistance of the stainless steel strip 3 is almost negligible.

〈発明の効果〉 以上の説明から明らかなように、本発明にかかるステン
レス帯鋼の電解処理袋とによれば、電解槽(横型)の入
側においてはステンレス帯鋼の上下両面に対設した陽電
極と陰電極間に電流が流れるため、はぼ電解液抵抗のみ
となり、帯鋼抵抗はほとんど無視できる程度に小さく、
出側では電極ロールを採用していることにより、電気回
路が一組になっているので電解液抵抗が小さくでき、装
置に要する電源電圧を小さくすることができる結果、電
解処理に要する電力を大幅に節減することができる。
<Effects of the Invention> As is clear from the above description, according to the electrolytic treatment bag for stainless steel strip according to the present invention, on the entry side of the electrolytic tank (horizontal type), the bag for electrolytic treatment of stainless steel strip is provided oppositely on both the upper and lower surfaces of the stainless steel strip. Since current flows between the positive and negative electrodes, only the electrolyte resistance exists, and the resistance of the steel strip is so small that it can be ignored.
By using an electrode roll on the output side, the electric circuit is combined into one set, which reduces the resistance of the electrolyte and reduces the power supply voltage required for the device, resulting in a significant reduction in the power required for electrolytic treatment. savings can be made.

さらに、電極ロールが電解液中に浸漬されないので、装
置の構造が簡単になり、回転シール部からの液洩れ、電
浬ロールの表面性状の悪化に対する保守点検が軽減でき
る利点もある。
Furthermore, since the electrode roll is not immersed in the electrolytic solution, the structure of the device is simplified, and there is also the advantage that maintenance and inspection for liquid leakage from the rotating seal portion and deterioration of the surface quality of the electrolytic roll can be reduced.

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

第1図は本発明の実施例のステンレス帯鋼の電解処理装
置の概略構成を示す要部縦断面図、第2図は従来のステ
ンレス帯鋼の電解処理装置を構成を示す要部縦断面図で
ある。 図中、A・・・ステンレス帯鋼の入側、B・・・出側、
1・・・電解槽、2・・電解液、3・・・ステンレス帯
鋼、4・・・陽電極、5・・・陰電極、8・・・陽電極
、9・・・陰電極、11・・陰電極、13・・・コンダ
クタロール。
Fig. 1 is a longitudinal cross-sectional view of main parts showing a schematic configuration of an electrolytic treatment apparatus for stainless steel strip according to an embodiment of the present invention, and Fig. 2 is a longitudinal cross-sectional view of main parts showing the structure of a conventional electrolytic treatment apparatus for stainless steel strip. It is. In the diagram, A...inlet side of stainless steel strip, B...outlet side,
DESCRIPTION OF SYMBOLS 1... Electrolytic cell, 2... Electrolyte, 3... Stainless steel strip, 4... Positive electrode, 5... Negative electrode, 8... Positive electrode, 9... Negative electrode, 11 ...Cathode electrode, 13...Conductor roll.

Claims (1)

【特許請求の範囲】[Claims] 横型電解槽に入れた濃硫酸電解液中に浸漬されて走行す
るステンレス帯鋼の入側上下面にそれぞれ対向して配設
された互いに反対極性の対の電極を複数組、当該ステン
レス帯鋼の長さ方向に沿って順次配設する一方、ステン
レス帯鋼の出側上下面にそれぞれ、陰電極を対にして対
向配設すると共に、横型電解槽の出側外部に、ステンレ
ス帯鋼を誘導する陽極性の電極ロールを設けたことを特
徴とするステンレス帯鋼の電解処理装置。
A plurality of pairs of electrodes with opposite polarities are arranged facing each other on the upper and lower surfaces of the entrance side of a stainless steel strip that is immersed in a concentrated sulfuric acid electrolyte solution placed in a horizontal electrolytic tank and runs. While disposing them sequentially along the length direction, negative electrodes are arranged in pairs on the upper and lower surfaces of the outlet side of the stainless steel strip, respectively, and facing each other, and the stainless steel strip is guided to the outside of the outlet side of the horizontal electrolytic cell. An electrolytic treatment device for stainless steel strip, characterized by being equipped with an anodic electrode roll.
JP30553186A 1986-12-23 1986-12-23 Apparatus for electrolytically treating stainless band steel Pending JPS63161197A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30553186A JPS63161197A (en) 1986-12-23 1986-12-23 Apparatus for electrolytically treating stainless band steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30553186A JPS63161197A (en) 1986-12-23 1986-12-23 Apparatus for electrolytically treating stainless band steel

Publications (1)

Publication Number Publication Date
JPS63161197A true JPS63161197A (en) 1988-07-04

Family

ID=17946271

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30553186A Pending JPS63161197A (en) 1986-12-23 1986-12-23 Apparatus for electrolytically treating stainless band steel

Country Status (1)

Country Link
JP (1) JPS63161197A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102061510A (en) * 2010-06-29 2011-05-18 常州市正成标牌设备有限公司 Electrolytic etching method of metal plate and etching machine thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102061510A (en) * 2010-06-29 2011-05-18 常州市正成标牌设备有限公司 Electrolytic etching method of metal plate and etching machine thereof

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