JPH0356699A - Method and device for descaling strip - Google Patents

Method and device for descaling strip

Info

Publication number
JPH0356699A
JPH0356699A JP18879389A JP18879389A JPH0356699A JP H0356699 A JPH0356699 A JP H0356699A JP 18879389 A JP18879389 A JP 18879389A JP 18879389 A JP18879389 A JP 18879389A JP H0356699 A JPH0356699 A JP H0356699A
Authority
JP
Japan
Prior art keywords
strip
steel
electrolytic
electrolyte
descaling
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
JP18879389A
Other languages
Japanese (ja)
Inventor
Keiji Yamamoto
啓二 山本
Kazuto Kaneshige
和人 兼重
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 Heavy Industries Ltd
Original Assignee
Sumitomo 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP18879389A priority Critical patent/JPH0356699A/en
Publication of JPH0356699A publication Critical patent/JPH0356699A/en
Pending legal-status Critical Current

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  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

PURPOSE:To efficiently descale the surface of a band steel by using the steel as an anode, injecting an electrolyte from a cathode plate provided above and below the steel to renew the electrolyte on the steel surface, stably passing the steel through the center between the cathodes and applying a current. CONSTITUTION:The band steel 4 having scales on its surface is passed through a neutral electrolyte 2 of Na2SO4, etc., in an electrolytic cell 1 by conductor rolls 3 and 3'. The steel 4 is used as an anode through a DC power source 7 and traveled between the cathodes 5 and 5' set in the electrolyte 2, and a current is applied. Many electrolyte injection ports are provided on the surface of the cathodes 5 and 5' facing the steel 4, the electrolyte is circulated by a pump 11 and injected from the injection ports of the cathodes 5 and 5', and the steel 4 is smoothly traveled by the liq. pressure without itself being brought into contact with the cathodes 5 and 5'. Since the fresh electrolyte is constantly supplied to the surface of the steel 4, the scales on the surface of the steel 4 are uniformly removed at a high rate.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明はストリップの電解ディスケーリング方法及び
装置、殊にステンレス鋼板の中性塩電解によるディスケ
ーリング方法及び装置に関するものである. [従来の技術] 従来より電解液中にストリップを通板して脱スケールを
行なう、所謂電解ディスケーリング方法は公知である. しかし乍ら、従来の電解ディスケーリング方法及び装置
は、第4図及び第5図に示す如く、電解液2を充填した
電解層1の入側と出側に夫々シンクロール20.20’
を設けると共に、該ロール20.20’間に複数対のサ
ポートロ〜ル21を設け、かつ、該サポートロール21
を挟んで交互に陰i電極対22.22’と陽極電極対2
3.23’とを配置した構成とし、ストリップ4をサポ
ートロール20,20’により支持しながら電極液2中
に通板する過程で陽極電極23.23’からストリップ
4を介して陰極電極22.22’に流れる電解電流によ
ってストリップ表面の脱スケールを行なうようになって
いる. [発明が解決しようとする課題] 従来の電解ディスケーリング方法及び装置は、電解液2
中をサポートロール21によって支持されて通板される
ストリップ4にサポートロール21を挟んで交互に配設
した陽極電極23.23’からストリップ4を介して陰
極電極22.22’に流れる電解電流によって脱スケー
ルを行なうものであるため、構戒上、サボトロール21
と陽極t極23.23’及び陰極電極22.22’は必
要不可欠であり、これらを配置する入側と出側のシンク
ロール20.20′の間隔を大きくとらざるを得す、大
きな電解層1が必要であると共に多量の電解液2も必要
となる等、装置自体が大型化することを避けられなかっ
た. また、電解層1中のストリップ4はサポートロール21
によって支持されているものの、サポートロール2l相
互間はフリーであり、この間で通板中のストリップ4が
波打ちを起すと電極22.22’及び23.23’とス
トリップ4との間隙が変化するため、電解電流を大きく
して最大間隙時にも十分な電解電流を確保できるように
しなければならずランニングコストも嵩む結果となって
いた。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method and apparatus for electrolytic descaling of a strip, and in particular to a method and apparatus for electrolytic descaling of a stainless steel plate by neutral salt electrolysis. [Prior Art] The so-called electrolytic descaling method, in which descaling is performed by passing a strip through an electrolytic solution, is well known. However, the conventional electrolytic descaling method and apparatus, as shown in FIGS. 4 and 5, have sink rolls 20 and 20' on the inlet and outlet sides of the electrolyte layer 1 filled with the electrolytic solution 2, respectively.
A plurality of pairs of support rolls 21 are provided between the rolls 20 and 20', and the support rolls 21
Negative i-electrode pair 22, 22' and anode electrode pair 2 are alternately sandwiched between
3.23' are arranged, and in the process of passing the strip 4 into the electrode solution 2 while being supported by the support rolls 20, 20', the cathode electrode 22. The strip surface is descaled by the electrolytic current flowing through 22'. [Problem to be solved by the invention] The conventional electrolytic descaling method and device
The electrolytic current flows from the anode electrodes 23.23' alternately arranged across the support roll 21 to the cathode electrodes 22.22' via the strip 4 through the strips 4 supported by the support rolls 21. Because it descales, sabotroll 21
The anode T electrode 23.23' and the cathode electrode 22.22' are indispensable, and it is necessary to keep a large distance between the sink rolls 20.20' on the inlet and outlet sides where they are arranged, and to create a large electrolytic layer. 1 and a large amount of electrolyte 2 are also required, which inevitably increases the size of the device itself. Further, the strip 4 in the electrolytic layer 1 is connected to a support roll 21.
However, the space between the support rolls 2l is free, and if the strip 4 that is being passed between these rolls becomes wavy, the gap between the electrodes 22, 22' and 23, 23' and the strip 4 will change. However, the electrolytic current must be increased to ensure a sufficient electrolytic current even at the maximum gap, resulting in increased running costs.

し課題を解決するための手段] 本発明によれば、電解液中にストリップを連続的に通板
しながら脱スケールを行なう電解ディスケーリング方法
において、電解層の入側と出側に陽極となるコンダクタ
ロールを設けると共に、該ロール間にストリップの通板
経路を挟んで対向する少くとも一対の陰極電極を設け、
かつ、該陰極電極には夫々流体噴出孔を設けて、該流体
噴出孔から噴出する流体圧によってストリップを陰f!
電極間の略中央に保持しながら入側コンダクタロール側
から出側コンダクタロール側に通板するようにしたこと
を特徴とするストリップのデイスゲーリング゜方法、及
び電解液中にストリップを連続的に通板しながら脱スケ
ールを行なう電解デイスケーリング装置において、電解
層の入側と出側に陽極電源に接続したコンダクタロール
を設けると共に、該ロール間に電解液中に浸るようにス
トリップの通板経路を挟んで対向する少く共一対の陰極
電源に接続した陰極電極を設け、かつ、該陰極電極には
ストリップの通板経路に向って開口した流体噴出孔を設
けたことを特徴とするストリップのディスケーリング装
置が得られる. [発明の作用] 本発明によれば、従来のシンクロール20.20′に代
えて陽極電源に接続したコンダクタロール3.3′とし
て、該ロール3.3′を陽極電極とし、該電極からスト
リップ4を介して電解液2中に配設した陰極電極5.5
′に向って直接電解電流を通電する. また、ストリップ4は陰極電極5,5′に設けた流体噴
出孔9.9′からの流体圧によって陰極電極5.5′間
の略中央に安定して保持されるので、陰極電極5.5′
間で通板中のストリップ4が波打ちを生じるために発生
する接触トラブルもない. [実施例] 以下、第1図乃至第3に示した実施例に沿い説明する. 第1図において、1は電解層で、該電解層の入側と出側
には夫々中性塩電解液等の電解液2中に一部を浸漬した
コンダクタロール3.3′が配設されている. そして、このコンダクタロール3.3′間には前記電解
液2中に浸るように、前記コンダクタロール3.3′を
結ぶストリップ4の移動経路を挟んで対称に二対の陰極
電極4.4′が設けられている. 5.5′は前記電解層1外部の入側と出側に夫々設けた
デフレクタロールで、入側デフレクタロール5を介して
ストリップ4を電解層1内に導びき、出側デフレクタロ
ール6′を介して電解層1から送出するようになってい
る.第2図を併せて参照して、前記コンダクタロール3
.3′と陰極電極5.5′は電源装置7の陽極側にコン
ダクタロール3,3′側を陰極側に陰極電極5,5′を
接続して゛いる.第3図を併せて参照して、前記陰極電
極5,5′のストリップ4通板経路の反対側には夫々ジ
ャケット8.8′が設けられると共に、ストリップ4通
板経路側には流体噴出孔9.9′が開口している. この流体噴出孔9.9′はストリップ4と略直交させて
1個或いは複数個の孔をストリップ4の通板経路中央に
沿って若しくは、ストリップ4の通板経路中心を挟んで
千鳥状に配置しても良いが、この流体噴出孔9,9′は
望ましくは夫々の陰極電極5,5′にストリップの幅方
向に向って交差する一対、或いは複数対の孔9,9′と
し、対向する孔から噴出した流体の一部をストリップ4
と陰極電極5,5′との間に閉じ込み流体クッション部
10.10’を形或させる. 11.11’はポンプで、サブタンク12と前記ジャケ
ット8.8′とを連結する配管l313′中に設けられ
ている. なお、このポンプ11.11’は、前記流体クッション
部10.10’のクッション圧力をコントロールするた
めに可変吐出量ポンプとするか、固定吐出量ポンプとし
た場合、配管13.13′中に図示しない流量制御弁を
介装するのが望ましい。
Means for Solving the Problem] According to the present invention, in an electrolytic descaling method in which descaling is performed while a strip is continuously passed through an electrolytic solution, an anode is provided on the inlet and outlet sides of the electrolytic layer. providing a conductor roll, and providing at least a pair of cathode electrodes facing each other across the strip passing path between the rolls;
Further, each of the cathode electrodes is provided with a fluid ejection hole, and the strip is heated by the fluid pressure ejected from the fluid ejection hole.
A method for disgaling a strip, which is characterized in that the strip is passed from the inlet conductor roll side to the outlet conductor roll side while being held approximately in the center between the electrodes, and the strip is continuously passed through an electrolytic solution. In an electrolytic dayscaling device that performs descaling while stripping, conductor rolls connected to an anode power source are provided on the inlet and outlet sides of the electrolytic layer, and a strip passing path is provided between the rolls so that the strip is immersed in the electrolyte. Descaling of a strip characterized by providing cathode electrodes connected to at least a pair of cathode power supplies facing each other, and the cathode electrodes being provided with fluid ejection holes opening toward the strip passage path. The device is obtained. [Operation of the Invention] According to the present invention, a conductor roll 3.3' connected to an anode power source is used instead of the conventional sink roll 20.20', and the roll 3.3' is used as an anode electrode, and a strip is removed from the electrode. cathode electrode 5.5 disposed in electrolyte 2 via 4
Electrolytic current is applied directly toward ′. In addition, the strip 4 is stably held approximately in the center between the cathode electrodes 5.5' by the fluid pressure from the fluid jet holes 9.9' provided in the cathode electrodes 5, 5'. ′
There is no contact trouble caused by the waving of the strip 4 during threading between the strips. [Example] The following is an explanation based on the example shown in FIGS. 1 to 3. In FIG. 1, reference numeral 1 denotes an electrolytic layer, and conductor rolls 3 and 3' partially immersed in an electrolytic solution 2 such as a neutral salt electrolytic solution are disposed on the inlet and outlet sides of the electrolytic layer, respectively. ing. Between the conductor rolls 3.3', two pairs of cathode electrodes 4.4' are arranged symmetrically across the moving path of the strip 4 connecting the conductor rolls 3.3' so as to be immersed in the electrolyte 2. is provided. Denoted at 5.5' are deflector rolls provided on the inlet and outlet sides of the electrolyte layer 1, respectively, which guide the strip 4 into the electrolyte layer 1 via the inlet deflector roll 5, and guide the strip 4 into the electrolyte layer 1 through the outlet deflector roll 6'. It is designed to be sent from the electrolytic layer 1 through the electrolytic layer 1. Referring also to FIG. 2, the conductor roll 3
.. 3' and cathode electrodes 5 and 5' connect the conductor rolls 3 and 3' to the anode side of the power supply 7, and the cathode electrodes 5 and 5' to the cathode side. Referring also to FIG. 3, jackets 8 and 8' are provided on the opposite side of the strip 4 passage of the cathode electrodes 5 and 5', and fluid jet holes are provided on the side of the strip 4 passage. 9.9' is open. The fluid ejection holes 9,9' are arranged approximately perpendicularly to the strip 4, and one or more holes are arranged along the center of the threading path of the strip 4 or in a staggered manner with the center of the threading path of the strip 4 sandwiched therebetween. However, the fluid ejection holes 9, 9' are preferably a pair of holes 9, 9' that intersect with each other in the width direction of the strip in the respective cathode electrodes 5, 5', and are opposed to each other. A portion of the fluid ejected from the hole is removed from the strip 4.
A confined fluid cushion portion 10, 10' is formed between the cathode electrodes 5 and 5'. 11.11' is a pump, which is installed in the pipe 1313' that connects the sub-tank 12 and the jacket 8.8'. Note that this pump 11.11' may be a variable displacement pump to control the cushion pressure of the fluid cushion portion 10.10' or a fixed displacement pump, as shown in the diagram in the piping 13.13'. It is desirable to install a flow control valve that does not.

次に、本発明のデイスケーリング作用について説明する
. 電解層1内にストリップ4を通板しながら電流を流すと
、電流はコンダクタロール3,3′からストリップ4を
経て電解液2中を通って陰極電極5.5′に流れる. 従って、ストリップ4を陽極とした電解反応によってス
トリップ4の表面に付着したスケルが取除かれる. この時、硫酸ナトリウム(Na2 SO4)等の中性塩
の電解液中でステンレス鋼板の脱スケールを行なう場合
、その電解反応は、 + Cr2(h +5H20 − 2Cr04 +10H 
+6e・111Cr20g +  4}120 4 C
r20−7− + 88++6e−(2)という酸素発
生反応が、また陰極側では、2hO + 2e −  
H2 + 20HT:−++・・−+・・・・−+・−
f4)という水素発生反応が二次的に生ずる.この電解
反応中に生する+12及び02がストリップ4と陰極電
極5.5′との間に充満すると遮断抵抗電圧が増大する
ことになるが、本発明では、陰極電極5.5′に流体噴
出孔9.9′を設けてストリップ4と陰極電極5.5′
との間の電解液2を強制的に循環させているので、H2
及び02の排出は迅速に行なえる. 従って、ストリップ4と陰極電極5,5′との間の電解
液2の濃度は常時略一定に保持できるので、安定した電
解反応を行なわせることができる. しかも、本発明では、コンダクタロール3.3′から直
接ストリップ4に通電するので、従来の陽極→電解層→
ストリップという通電方式に比較して陽極側での電解液
2による電圧降下を生じることがないと共に、ストリッ
プ4と陰極電極5,5′との間は流体クッションによっ
て鋼板の波打ちを防止して常時、略一定の間隔に保持す
るので、電解電流の密度も均一に保持できる. [発明の効果] 本発明によれば、従来の陽極電極及びサボトロールを省
略できるから装置を小型化できると共に、ストリップと
陰極電極との間隔を常時一定に保持すると共に、特に中
性塩電解の際に発生するH2或いは02がストリップと
陰極電極との間に滞溜しないようにこの部分の電解液を
強制的に循環させるので、電解液からの発生ガスによる
遮断抵抗電圧の増大やストリップの波打ちによる電解電
流の不均一も防止できるので電解ディスケーリング効率
の向上を図り得ると共に、消費電力も低減できるので、
ランニングコストも低く押えられる等の効果を有する。
Next, the day scaling effect of the present invention will be explained. When a current is passed through the electrolytic layer 1 while passing the strip 4, the current flows from the conductor rolls 3, 3', through the strip 4, through the electrolytic solution 2, and to the cathode electrode 5.5'. Therefore, the scale attached to the surface of the strip 4 is removed by an electrolytic reaction using the strip 4 as an anode. At this time, when descaling a stainless steel plate in an electrolytic solution of a neutral salt such as sodium sulfate (Na2 SO4), the electrolytic reaction is + Cr2 (h +5H20 - 2Cr04 +10H
+6e・111Cr20g + 4}120 4 C
The oxygen evolution reaction r20-7- + 88++6e-(2) occurs, and on the cathode side, 2hO + 2e-
H2 + 20HT: −++・・−+・・・−+・−
A hydrogen generating reaction called f4) occurs secondarily. If +12 and 02 generated during this electrolytic reaction fill between the strip 4 and the cathode electrode 5.5', the cutoff resistance voltage will increase. A hole 9.9' is provided to connect the strip 4 and the cathode electrode 5.5'.
Since the electrolyte 2 is forcibly circulated between the H2
and 02 can be discharged quickly. Therefore, the concentration of the electrolytic solution 2 between the strip 4 and the cathode electrodes 5, 5' can be kept substantially constant at all times, so that a stable electrolytic reaction can be carried out. Moreover, in the present invention, since current is applied directly to the strip 4 from the conductor roll 3, 3', the conventional anode→electrolytic layer→
Compared to the strip energization method, there is no voltage drop caused by the electrolyte 2 on the anode side, and a fluid cushion between the strip 4 and the cathode electrodes 5, 5' prevents the steel plate from waving, so that Since they are kept at approximately constant intervals, the density of the electrolytic current can also be kept uniform. [Effects of the Invention] According to the present invention, the conventional anode electrode and sabotroll can be omitted, so the device can be made smaller, and the distance between the strip and the cathode electrode can be kept constant at all times. The electrolyte in this area is forcibly circulated so that the H2 or 02 generated in the strip does not accumulate between the strip and the cathode electrode. Since non-uniformity of electrolytic current can be prevented, electrolytic descaling efficiency can be improved, and power consumption can also be reduced.
This has the effect of keeping running costs low.

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

第1図は本発明の概略図.第2図は同配線系統図,第3
図は第1図の■〜線に沿う断面図,第4図は従来の電解
ディスケーリング装置の一例を示す概略図,第5図は同
配線系統図である. 1・・・電解層        2・・・電解液3.3
′・・・コンダクタロール
Figure 1 is a schematic diagram of the present invention. Figure 2 is the same wiring system diagram, Figure 3
The figure is a sectional view taken along line 1 in Figure 1, Figure 4 is a schematic diagram showing an example of a conventional electrolytic descaling device, and Figure 5 is a wiring diagram of the same. 1... Electrolyte layer 2... Electrolyte solution 3.3
′・・・Conductor roll

Claims (1)

【特許請求の範囲】 1)電解液中にストリップを連続的に通板しながら脱ス
ケールを行なう電解ディスケーリング方法において、電
解層の入側と出側に陽極となるコンダクタロールを設け
ると共に、該ロール間にストリップの通板経路を挟んで
対向する少くとも一対の陰極電極を設け、か つ、該陰極電極には夫々流体噴出孔を設け て、該流体噴出孔から噴出する流体圧によつてストリッ
プを陰極電極間の略中央に保持しながら入側コンダクタ
ロール側から出側コンダクタロール側に通板するように
したことを特徴とするストリップのディスケーリング方
法。 2)電解液中にストリップを連続的に通板しながら脱ス
ケールを行なう電解ディスケーリング装置において、電
解層の入側と出側に陽極電源に接続したコンダクタロー
ルを設けると共に、該ロール間に電解液中に浸るように
ストリップの通板経路を挟んで対向する少く共一対の陰
極電源に接続した陰極電極を設け、かつ、該陰極電極に
はストリップの通板経路に向って開口した流体噴出孔を
設けたことを特徴とするストリップのディスケーリング
装置。
[Claims] 1) In an electrolytic descaling method in which descaling is carried out while a strip is continuously passed through an electrolytic solution, conductor rolls serving as anodes are provided on the inlet and outlet sides of the electrolytic layer, and At least a pair of cathode electrodes are provided between the rolls, facing each other across the strip passing path, and each of the cathode electrodes is provided with a fluid ejection hole, and the strip is heated by the fluid pressure ejected from the fluid ejection hole. A method for descaling a strip, characterized in that the strip is passed from the inlet conductor roll side to the outlet conductor roll side while holding the strip approximately in the center between the cathode electrodes. 2) In an electrolytic descaling device that performs descaling while continuously passing a strip through an electrolytic solution, conductor rolls connected to an anode power supply are provided on the inlet and outlet sides of the electrolytic layer, and an electrolytic At least a pair of cathode electrodes connected to a cathode power supply are provided, which are immersed in the liquid and facing each other across the strip passing path, and each cathode electrode has a fluid ejection hole opened toward the strip passing path. A strip descaling device characterized in that it is provided with.
JP18879389A 1989-07-24 1989-07-24 Method and device for descaling strip Pending JPH0356699A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18879389A JPH0356699A (en) 1989-07-24 1989-07-24 Method and device for descaling strip

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18879389A JPH0356699A (en) 1989-07-24 1989-07-24 Method and device for descaling strip

Publications (1)

Publication Number Publication Date
JPH0356699A true JPH0356699A (en) 1991-03-12

Family

ID=16229898

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18879389A Pending JPH0356699A (en) 1989-07-24 1989-07-24 Method and device for descaling strip

Country Status (1)

Country Link
JP (1) JPH0356699A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0870854A1 (en) * 1997-04-10 1998-10-14 Hotani Co., Ltd. Method and apparatus for cleaning strips
US6325913B1 (en) 1998-08-24 2001-12-04 Hitachi, Ltd. Steel strip descaling apparatus and a steel strip manufacturing apparatus using the descaling apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0870854A1 (en) * 1997-04-10 1998-10-14 Hotani Co., Ltd. Method and apparatus for cleaning strips
US6216304B1 (en) 1997-04-10 2001-04-17 Hotani Co., Ltd. Apparatus for cleaning strips
US6325913B1 (en) 1998-08-24 2001-12-04 Hitachi, Ltd. Steel strip descaling apparatus and a steel strip manufacturing apparatus using the descaling apparatus
US6726830B2 (en) 1998-08-24 2004-04-27 Hitachi, Ltd. Steel strip descaling apparatus and a steel strip manufacturing apparatus using the descaling apparatus

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