JPS6333600A - Method for electrolytically pickling steel strip - Google Patents

Method for electrolytically pickling steel strip

Info

Publication number
JPS6333600A
JPS6333600A JP17665786A JP17665786A JPS6333600A JP S6333600 A JPS6333600 A JP S6333600A JP 17665786 A JP17665786 A JP 17665786A JP 17665786 A JP17665786 A JP 17665786A JP S6333600 A JPS6333600 A JP S6333600A
Authority
JP
Japan
Prior art keywords
pickling
steel strip
plates
steel
anode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP17665786A
Other languages
Japanese (ja)
Other versions
JPH0535240B2 (en
Inventor
Yasushi Sawairi
澤入 泰
Masatsugu Horishita
堀下 昌嗣
Kazuhiro Tano
和広 田野
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP17665786A priority Critical patent/JPS6333600A/en
Publication of JPS6333600A publication Critical patent/JPS6333600A/en
Publication of JPH0535240B2 publication Critical patent/JPH0535240B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To carry out perfect pickling and to obtain a steel strip having a fine surface when oxide on the surface of a steel strip is removed by electrolytic pickling in a pickling soln., by arranging anode plates and cathode plates having different lengths in the pickling soln. so that they confront each other on both sides of the steel strip which is passed through the pickling soln. CONSTITUTION:When an oxide film sticking to the surface of a steel strip 3 of ordinary steel, stainless steel or other steel is removed by passing the steel strip 3 through a pickling bath 2 such as a soln. of sulfuric acid, hydrochloric acid or phosphoric acid, pairs of anode plates 6 and cathode plates 7 are alternately arranged in the pickling bath 2 so that they confront each other on both sides of the steel strip 2 which is passed through the bath. In case of anodic pickling, the cathode plates 7 are made longer than the anode plates 6. In case of cathodic pickling, the anode plates 6 are made longer than the cathode plates 7. Unpickled parts are not present on the surface of the steel strip and a smooth fine pickled surface is obtd.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は普通低炭素鋼板、ステンレス鋼板など鋼ストリ
ップの電解酸洗法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a process for electrolytic pickling of steel strips, such as ordinary low carbon steel sheets and stainless steel sheets.

[従来の技術] 酸洗は高温加工や熱処理によって表面に生じたスケール
(酸化膜)を除去する際に行われるが、ステンレス鋼板
や塗装用あるいはメツキ用原板のように表面光沢素材と
して供される鋼ストリップは、酸洗を短時間に完了させ
て表面の変質や酸洗脆性を防止するため、陽極的酸洗法
または陰極的酸洗法の電解酸洗法が一般に採用されてい
る。その電解酸洗方法は、例えば実公昭58−3565
9号公報の第1図で紹介されているように、酸洗液中を
走行する鋼ストリップの上下に多数の電極板を該ストリ
ップの走行方向と直角となすように配列して通電し、脱
スケールを行うものである。
[Prior art] Pickling is performed to remove scale (oxide film) formed on the surface due to high-temperature processing or heat treatment, but it is also used as a material with a glossy surface, such as stainless steel sheets and base plates for painting or plating. In order to complete pickling in a short time and prevent surface deterioration and pickling embrittlement, steel strips are generally subjected to electrolytic pickling methods such as anodic pickling or cathodic pickling. The electrolytic pickling method is described in Japanese Utility Model Publication No. 58-3565, for example.
As introduced in Figure 1 of Publication No. 9, a large number of electrode plates are arranged above and below a steel strip running in a pickling solution so as to be perpendicular to the running direction of the strip, and are energized. It is a scale.

また鋼ストリップを対向する位置に配置される2枚1対
(組)の陽極板また陰極板を交互に鋼ストリップの走行
方向に配列したした電解酸洗方法もある。さらにこのよ
うな電解酸洗方法には、#4ストリップの板面に酸洗液
を強制流動させるために特公昭57−45319号公報
のように電極板の近傍に羽根車を設けたり、前記した公
報のように電極板の部分形状を変化させる試みもされて
いる。
There is also an electrolytic pickling method in which a pair (set) of anode plates or cathode plates are arranged at opposite positions of the steel strip and alternately arranged in the running direction of the steel strip. Furthermore, such an electrolytic pickling method includes the provision of an impeller near the electrode plate as in Japanese Patent Publication No. 57-45319 in order to forcefully flow the pickling liquid onto the plate surface of the #4 strip, and the method described above. Attempts have also been made to change the partial shape of the electrode plate, as disclosed in the publication.

[発明が解決しようとする問題点] このように電解酸洗法は、改善されている。しかしなが
ら酸洗を終えた鋼ストリップの表面には。
[Problems to be Solved by the Invention] As described above, the electrolytic pickling method has been improved. However, on the surface of the steel strip after pickling.

酸洗液中に溶解した不純物(Ni、 Cu、 Cr、 
Feなどの金属酸化物、水酸化物など)が電析し、酸洗
効率を著しく低下せしめる問題があった。本発明は酸洗
効率のよい電解酸洗法に関するもので、本発明者らは、
この問題を解決するために電解酸洗方法について種々検
討した結果、両極併用の利点から同一大きさに製作され
ている電極の大きさを電解法によって変えることにより
、問題解決されることを知見した。本発明はこの知見に
基づいて構成したものである。
Impurities dissolved in the pickling solution (Ni, Cu, Cr,
There was a problem in that metal oxides such as Fe, hydroxides, etc.) were deposited, significantly reducing the pickling efficiency. The present invention relates to an electrolytic pickling method with high pickling efficiency, and the present inventors have
As a result of various studies on electrolytic pickling methods to solve this problem, we found that the problem could be solved by changing the size of the electrodes, which are manufactured to the same size, using the electrolytic method due to the advantage of using both electrodes together. . The present invention was constructed based on this knowledge.

[間屈点を解決するための手段] 本発明は酸洗液中を走行する鋼ストリップを介して対向
する位置に配置される2枚1組の極板長さの異なる陽極
板と陰極板で、陽極的酸洗の場合は陽極板の長さを、ま
た陰極的酸洗の場合は陰極板の長さを他の極性の極板長
さよりも短かくして、鋼ストリップの走行方向に陽極板
及び陰極板を交互に配列したことを特徴とする鋼ストリ
ップの電解酸洗法である。
[Means for solving the bending point problem] The present invention uses a set of two plates, an anode plate and a cathode plate having different lengths, which are arranged at opposing positions across a steel strip running in a pickling solution. , the length of the anode plate in the case of anodic pickling and the length of the cathode plate in the case of cathodic pickling is shorter than the plate length of the other polarity, and the anode plate and the plate are arranged in the running direction of the steel strip. This is an electrolytic pickling method for steel strip characterized by alternately arranging cathode plates.

以下1本発明について図面を参照しながら詳細に説明す
る。
The present invention will be described in detail below with reference to the drawings.

図は本発明の一実施例を陽極的電解酸洗装置で示す。1
は処理槽で、酸洗液2が満たされている。
The figure shows an embodiment of the invention in an anodic electrolytic pickling apparatus. 1
is a processing tank filled with pickling liquid 2.

酸洗液2には硫酸系、塩酸系、燐酸系、その他の一般に
使用されている電解酸洗液を使用する。3は怜通低炭素
鋼、ステンレス鋼などの鋼ストリップである。4はデフ
レクタ−ロール、5はシールロールである。すなわち鋼
ストリップ3が電解処理槽1内をデフレクタ−ロール4
とシールロール5に案内されながら通過するように構成
されている。6は陽極板で7は陰極板である。陽極板6
と陰極板7はそれぞれ鋼ストリップ3を介して相対向す
る位置に配置される2枚1対(組)であり、かつ陽極板
6と陰極板7とは電極板の長さが異なり、鋼ストリップ
3の走行方向に交互に配列している。この場合陽極的酸
洗法においては陽極板6の長さは陰極板7より短く、ま
た陰極的酸洗法においては陰極板の長さは陽極板より短
くする。図は陽極的酸洗法で陽極板の長さを陰極板より
も短くした例を示す。
As the pickling solution 2, a sulfuric acid-based, hydrochloric acid-based, phosphoric acid-based, or other commonly used electrolytic pickling solution is used. 3 is a steel strip made of low carbon steel, stainless steel, etc. 4 is a deflector roll, and 5 is a seal roll. That is, the steel strip 3 is passed through the electrolytic treatment tank 1 by the deflector roll 4.
It is configured so that it passes while being guided by the seal roll 5. 6 is an anode plate and 7 is a cathode plate. Anode plate 6
The and cathode plates 7 are a pair (set) of two plates arranged opposite to each other with the steel strip 3 in between, and the anode plate 6 and the cathode plate 7 have different lengths, and the steel strip 3 are arranged alternately in the running direction. In this case, in the anodic pickling method, the length of the anode plate 6 is shorter than the cathode plate 7, and in the cathodic pickling method, the length of the cathode plate is shorter than the anode plate. The figure shows an example in which the length of the anode plate is shorter than the length of the cathode plate using the anodic pickling method.

[作用] 本発明者等は、各陽極板の長さQ+と各陰極板の長さQ
−を種々かえて鋼板の脱スケール酸洗効率を調査した。
[Function] The inventors have determined that the length Q+ of each anode plate and the length Q of each cathode plate
- The descaling pickling efficiency of steel plates was investigated by changing various values.

即ち L+(各陽極板の長さの総長)=ΣΩ+L−(各陰極板
の長さの総長)=Σ2−で、 L++ L−= 100
0 m (一定)で行った。
That is, L+ (total length of each anode plate) = ΣΩ + L- (total length of each cathode plate) = Σ2-, and L++ L- = 100
0 m (constant).

イ、総通電時間・・・50秒 口、酸洗液−H2SO4:200g/Q、NaN0.:
200g/Q、温度二80℃ ハ、陰極板の電流密度・・・40 A / d+m”二
、鋼ストリップ・・・5US409ホットコイル厚さ:
1.51m!1.巾:12゜ O+n+a、長さ:コイル 脱スケール酸洗の結果を第1表に示した。
A. Total energization time...50 seconds, pickling solution - H2SO4: 200g/Q, NaN0. :
200g/Q, temperature 280℃ C, current density of cathode plate...40 A/d+m"2, steel strip...5 US409 hot coil thickness:
1.51m! 1. Width: 12°O+n+a, length: Coil Descaling pickling results are shown in Table 1.

(枠内%は脱スケールされた面積%) 第1表からL−=500m、L+=500mの従来の酸
洗例ではストリップ鋼板の表面の60%の面積は脱スケ
ールされているが不十分な酸洗で、L−が大きくなる程
脱スケールが進み、L−= 800my L+=200
mで完全に脱スケールされている。即ち陽極的酸洗法で
は陰極板の長さQ−を陽極板Q+よりも長くする事によ
り、従来は脱スケールが不十分なものが完全に脱スケー
ルできることとなる。
(The percentage in the frame is the percentage of descaled area.) From Table 1, in the conventional pickling example where L- = 500m and L+ = 500m, 60% of the surface area of the strip steel plate is descaled, but it is insufficient. During pickling, descaling progresses as L- becomes larger, L-=800my L+=200
It is completely descaled at m. That is, in the anodic pickling method, by making the length Q- of the cathode plate longer than the length Q+ of the anode plate, it is possible to completely descale what was conventionally insufficiently descaled.

本発明の作用を陽極的酸洗法の例で説明したが、陰極的
酸洗法の場合は、陽極板の長さQ+の方を長くすること
により、高能率に酸洗できることは明かである。
The effect of the present invention has been explained using the example of the anodic pickling method, but it is clear that in the case of the cathodic pickling method, pickling can be carried out with high efficiency by increasing the length of the anode plate Q+. .

[発明の効果] しかして本発明は、陽極板と陰極板に通電しながらそれ
ぞれの極板の狭隘な間隙内を通過する鋼ストリップ3を
陽極的酸洗と陰極的酸洗(またこの逆′の酸洗もあり得
る)を繰返し、酸洗中に未酸洗部分のない表面美麗な鋼
ストリップを製造する。
[Effects of the Invention] Accordingly, the present invention enables anodic pickling and cathodic pickling (or vice versa) of the steel strip 3 passing through the narrow gap between the anode plate and the cathode plate while energizing the anode plate and the cathode plate. ) is repeated to produce a steel strip with a beautiful surface and no unpickled parts during pickling.

特にステンレス鋼ストリップを酸洗した時、表面を美麗
にして耐食性を向上する。また上記のような本発明法に
おいて、陽極的酸洗法では最終電極に対極の陰極板を、
また陰極的酸洗法では最終電極に対極の陽極板を設ける
と酸洗効率が一層向上する。
Especially when pickling stainless steel strips, it makes the surface beautiful and improves corrosion resistance. In addition, in the method of the present invention as described above, in the anodic pickling method, a counter cathode plate is used as the final electrode,
In addition, in the cathodic pickling method, the pickling efficiency is further improved by providing a counter anode plate to the final electrode.

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

図は本発明の一実施例で陽極酸洗法の例を示す。 1:処理槽、2:酸洗液、3:鋼ストリップ、4:デフ
レクタ−ロール、5:シールロール、6:陽極板、7:
陰極板、
The figure shows an example of an anodic pickling method according to an embodiment of the present invention. 1: Treatment tank, 2: Pickling liquid, 3: Steel strip, 4: Deflector roll, 5: Seal roll, 6: Anode plate, 7:
cathode plate,

Claims (1)

【特許請求の範囲】[Claims] 酸洗液中を走行する鋼ストリップを介して対向する位置
に配置される2枚1組の極板長さの異なる陽極板と陰極
板で、陽極的酸洗の場合は陽極板の長さを、また陰極的
酸洗の場合は陰極板の長さを他の極性の極板長さよりも
短かくして、鋼ストリップの走行方向に陽極板及び陰極
板を交互に配列したことを特徴とする鋼ストリップの電
解酸洗法。
A pair of anode and cathode plates with different lengths are placed opposite each other across a steel strip running in the pickling solution.In the case of anodic pickling, the length of the anode plate is In the case of cathodic pickling, the length of the cathode plates is shorter than the length of the plates of other polarities, and the anode plates and cathode plates are arranged alternately in the running direction of the steel strip. electrolytic pickling method.
JP17665786A 1986-07-29 1986-07-29 Method for electrolytically pickling steel strip Granted JPS6333600A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17665786A JPS6333600A (en) 1986-07-29 1986-07-29 Method for electrolytically pickling steel strip

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17665786A JPS6333600A (en) 1986-07-29 1986-07-29 Method for electrolytically pickling steel strip

Publications (2)

Publication Number Publication Date
JPS6333600A true JPS6333600A (en) 1988-02-13
JPH0535240B2 JPH0535240B2 (en) 1993-05-26

Family

ID=16017411

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17665786A Granted JPS6333600A (en) 1986-07-29 1986-07-29 Method for electrolytically pickling steel strip

Country Status (1)

Country Link
JP (1) JPS6333600A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07113200A (en) * 1993-08-26 1995-05-02 Sumitomo Metal Mining Co Ltd Electrolytic polishing device and electrolyte thereof and electrolytic polishing method
EP0814180A1 (en) * 1996-06-19 1997-12-29 Keramchemie GmbH Process for treating stainless steel surfaces
KR100576045B1 (en) * 2001-12-26 2006-05-03 주식회사 포스코 Electrolytic pickling method of stainless steels
EP2133448A1 (en) * 2007-03-02 2009-12-16 The Furukawa Electric Co., Ltd. Production method and device of surface roughened copper plate, and surface roughened copper plate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS572800A (en) * 1980-05-05 1982-01-08 Mizuru Anri Drawing device
JPS5959900A (en) * 1982-09-29 1984-04-05 Kawasaki Steel Corp Continuous electrolytic descaling method of stainless steel strip

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS572800A (en) * 1980-05-05 1982-01-08 Mizuru Anri Drawing device
JPS5959900A (en) * 1982-09-29 1984-04-05 Kawasaki Steel Corp Continuous electrolytic descaling method of stainless steel strip

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07113200A (en) * 1993-08-26 1995-05-02 Sumitomo Metal Mining Co Ltd Electrolytic polishing device and electrolyte thereof and electrolytic polishing method
EP0814180A1 (en) * 1996-06-19 1997-12-29 Keramchemie GmbH Process for treating stainless steel surfaces
KR100576045B1 (en) * 2001-12-26 2006-05-03 주식회사 포스코 Electrolytic pickling method of stainless steels
EP2133448A1 (en) * 2007-03-02 2009-12-16 The Furukawa Electric Co., Ltd. Production method and device of surface roughened copper plate, and surface roughened copper plate
EP2133448A4 (en) * 2007-03-02 2011-04-27 Furukawa Electric Co Ltd Production method and device of surface roughened copper plate, and surface roughened copper plate
US8815072B2 (en) 2007-03-02 2014-08-26 Furukawa Electric Co., Ltd. Method for producing a surface roughened copper plate
US9758890B2 (en) 2007-03-02 2017-09-12 Furukawa Electric Co., Ltd. Production method and device of surface roughened copper plate, and surface roughened copper plate

Also Published As

Publication number Publication date
JPH0535240B2 (en) 1993-05-26

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