Nothing Special   »   [go: up one dir, main page]

JP2014181382A - Method of surface-treating metallic strip - Google Patents

Method of surface-treating metallic strip Download PDF

Info

Publication number
JP2014181382A
JP2014181382A JP2013056716A JP2013056716A JP2014181382A JP 2014181382 A JP2014181382 A JP 2014181382A JP 2013056716 A JP2013056716 A JP 2013056716A JP 2013056716 A JP2013056716 A JP 2013056716A JP 2014181382 A JP2014181382 A JP 2014181382A
Authority
JP
Japan
Prior art keywords
water
roll
surface treatment
metal strip
steel strip
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
JP2013056716A
Other languages
Japanese (ja)
Other versions
JP5821882B2 (en
Inventor
Yutaka Watanabe
裕 渡辺
Koji Kawasaki
浩司 川崎
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 Steel Corp
Original Assignee
JFE 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 JFE Steel Corp filed Critical JFE Steel Corp
Priority to JP2013056716A priority Critical patent/JP5821882B2/en
Publication of JP2014181382A publication Critical patent/JP2014181382A/en
Application granted granted Critical
Publication of JP5821882B2 publication Critical patent/JP5821882B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Electroplating Methods And Accessories (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a more effective technique for dissolving poor electric conduction caused by deposit adhered to a conduction roll.SOLUTION: A method of surface-treating a metallic strip includes a water scattering step of scattering water on a conduction roll which is arranged on the side of the inlet and/or the outlet of an electrolytic treatment tank of a surface treatment installation for carrying out surface treatment while carrying the metal strip and a surface treatment step of surface-treating the metal strip. The scattered water has a pH of 6.5-8.0. In the water scattering step, water is preferably scattered onto the metal strip so that the electrolyte concentration in recovered water is a half or lower of the electrolyte concentration in the electrolytic treatment tank, in recovering water adhered to the surface of the metal strip.

Description

本発明は、金属帯の表面を処理する表面処理方法に関する。   The present invention relates to a surface treatment method for treating the surface of a metal strip.

一般に金属帯の表面処理方法の一つとして、電解質溶液を満たした電解処理槽内で通電ロールを介して金属帯を負に帯電させ金属帯に目的とする金属を電解析出する方法が行われている。   In general, as one of the surface treatment methods for the metal strip, a method is used in which the metal strip is negatively charged via an energizing roll in an electrolytic treatment tank filled with an electrolyte solution, and the target metal is electrolytically deposited on the metal strip. ing.

このような方法で金属帯を表面処理した場合に、金属帯表面に析出した金属が後続の通電ロールに付着堆積して、通電不良が生じるという問題がある。   When the metal strip is surface-treated by such a method, there is a problem that the metal deposited on the surface of the metal strip adheres to and accumulates on the subsequent energizing roll, resulting in poor energization.

また、処理速度を速めるために電流密度を高くした場合、金属の酸化物が発生しやすい。この酸化物は金属に比べて電気抵抗が10倍程度大きいため、この酸化物が後続の通電ロールに堆積すると通電不良を生じる場合がある。   Further, when the current density is increased in order to increase the processing speed, metal oxides are likely to be generated. Since this oxide has an electric resistance that is about 10 times larger than that of metal, there may be a case where an energization failure occurs when this oxide is deposited on a subsequent energizing roll.

特許文献1には、通電ロールにおいて、上記通電不良を解消する技術が開示されている。具体的には、通電ロール上及び金属帯上の少なくとも一方に、酸又はアルカリ水溶液を散布する方法が記載されている。   Patent Document 1 discloses a technique for eliminating the above-described energization failure in an energizing roll. Specifically, a method of spraying an acid or alkaline aqueous solution on at least one of the current-carrying roll and the metal strip is described.

特開平04−17695号公報Japanese Patent Laid-Open No. 04-17695

特許文献1に記載の方法で、上記通電不良の問題を解消できるものの、特許文献1に記載の方法には、めっき層内に遮蔽板を設置する必要があり、設備スペースの制約や、遮蔽板とコンダクターロールや金属帯との接触の問題があり、工業的製造方法としては問題がある。そこで、この問題が生じず、より有効な方法があれば好ましい。   Although the method described in Patent Document 1 can solve the problem of the above-described poor conduction, the method described in Patent Document 1 requires the installation of a shielding plate in the plating layer, which limits the installation space and the shielding plate. There is a problem of contact between the conductor roll and the metal strip, and there is a problem as an industrial manufacturing method. Therefore, it would be desirable if there was a more effective method that would not cause this problem.

本発明は上記課題を解決するためになされたものであり、その目的は、通電ロールに付着する堆積物が原因として生じる通電不良を解消する従来より有効な技術を提供することにある。   The present invention has been made to solve the above-described problems, and an object of the present invention is to provide a technique that is more effective than the conventional technique that eliminates a current-carrying failure caused by deposits adhering to a current-carrying roll.

本発明者らは、上記課題を解決するために鋭意研究を重ねた。その結果、金属帯を搬送しながら表面処理する表面処理設備の電解処理槽の入側及び/又は出側に配置された通電ロール上に水を散布する水散布工程と、金属帯を表面処理する表面処理工程を有する方法であれば、上記課題を解決できることを見出し、本発明を完成するに至った。より具体的には本発明は以下のものを提供する。   The inventors of the present invention have made extensive studies to solve the above problems. As a result, a water spraying step of spraying water on the energizing rolls arranged on the entry side and / or exit side of the electrolytic treatment tank of the surface treatment facility that carries out the surface treatment while conveying the metal strip, and the metal strip is surface treated It has been found that the above problems can be solved by a method having a surface treatment step, and the present invention has been completed. More specifically, the present invention provides the following.

(1) 金属帯を搬送しながら表面処理する表面処理設備の電解処理槽の入側及び/又は出側に配置された通電ロール上に水を散布する水散布工程と、金属帯を表面処理する表面処理工程を有する表面処理方法。   (1) A water spraying step of spraying water on energizing rolls arranged on the entry side and / or exit side of an electrolytic treatment tank of a surface treatment facility for carrying out a surface treatment while conveying the metal strip, and surface treating the metal strip A surface treatment method having a surface treatment step.

(2) 前記水はpHが6.5〜8.0であり、前記水散布工程は、金属帯の表面に付着した水を回収したときに、回収された水中の電解質濃度が、前記電解処理槽中の電解質濃度の1/2以下になるように、水を金属帯に散布する工程である(1)に記載の表面処理方法。   (2) The water has a pH of 6.5 to 8.0, and when the water spraying step recovers the water adhering to the surface of the metal strip, the concentration of the electrolyte in the recovered water is the electrolytic treatment. The surface treatment method as described in (1) which is a process of spraying water on a metal strip so that it may become 1/2 or less of the electrolyte concentration in a tank.

本発明の方法によれば、通電ロールでの通電不良の発生を防止し、全体的に良好な外観を有する表面処理金属帯を製造できる。   According to the method of the present invention, it is possible to produce a surface-treated metal strip that prevents the occurrence of energization failure in the energizing roll and has an overall good appearance.

本発明の表面処理方法に使用可能な表面処理設備の一例を示す模式図である。It is a schematic diagram which shows an example of the surface treatment equipment which can be used for the surface treatment method of this invention. スプレー装置が通電ロールに水を散布する様子を示す模式図である。It is a schematic diagram which shows a mode that a spray apparatus sprays water on an electricity supply roll.

以下、本発明の実施形態について説明する。なお、本発明は以下の実施形態に限定されない。   Hereinafter, embodiments of the present invention will be described. In addition, this invention is not limited to the following embodiment.

先ず、本発明の表面処理方法に用いる表面処理設備について説明する。図1は、本発明の表面処理方法に使用可能な表面処理設備の一例を示す模式図である。図1に示す表面処理設備は、鋼帯表面に電気めっき処理を施すための水平型電気めっき設備であるが、本発明の方法には、鋼帯以外の金属帯を、水平型電気めっき設備以外の表面処理設備を用いて処理する方法も含まれる。   First, the surface treatment equipment used for the surface treatment method of the present invention will be described. FIG. 1 is a schematic view showing an example of surface treatment equipment that can be used in the surface treatment method of the present invention. The surface treatment facility shown in FIG. 1 is a horizontal electroplating facility for performing electroplating treatment on the surface of a steel strip. However, in the method of the present invention, a metal strip other than a steel strip can be used other than a horizontal electroplating facility. The method of processing using the surface treatment equipment is also included.

図1に示す水平型電気めっき設備1は、鋼帯2の表面に、電解質溶液3を用いて金属めっきを形成する設備である。   A horizontal electroplating facility 1 shown in FIG. 1 is a facility for forming metal plating on the surface of a steel strip 2 using an electrolyte solution 3.

図1に示す通り、水平型電気めっき設備1は、電解処理槽11と、電極12と、支持ロール13と、ダムロール14と、通電ロール15と、バックアップロール16と、通電ロール研磨装置17と、スプレー装置18とを備える。   As shown in FIG. 1, the horizontal electroplating equipment 1 includes an electrolytic treatment tank 11, an electrode 12, a support roll 13, a dam roll 14, an energizing roll 15, a backup roll 16, and an energizing roll polishing device 17 And a spray device 18.

電解処理槽11は、電解質溶液3を収容するための容器である。電解処理槽11に収容される電解質溶液3の種類は特に限定されず、所望の金属めっきを鋼帯2の表面に形成できるものを選択すればよい。例えば、金属イオンを含む硫酸浴、塩化物浴、及びこれらの混合浴等を用いることができる。   The electrolytic treatment tank 11 is a container for accommodating the electrolyte solution 3. The kind of the electrolyte solution 3 accommodated in the electrolytic treatment tank 11 is not particularly limited, and one that can form a desired metal plating on the surface of the steel strip 2 may be selected. For example, a sulfuric acid bath containing metal ions, a chloride bath, and a mixed bath thereof can be used.

本発明の表面処理方法は、亜鉛めっき処理に好ましく適用できるため、電解質溶液3は亜鉛めっきを鋼帯2の表面に形成するために、亜鉛イオンを含むことが好ましい。   Since the surface treatment method of the present invention can be preferably applied to galvanization treatment, the electrolyte solution 3 preferably contains zinc ions in order to form galvanization on the surface of the steel strip 2.

電極12は、電解処理槽11内を移動する鋼帯2の表面及び裏面に対向する位置に配置される。本実施形態において、鋼帯2の表面に対向する電極12と裏面に対向する電極12を一組の電極としたときに、電極12は電解処理槽11の前半部と後半部(鋼帯2の搬送方向の上流側と下流側)に二組設けられる。   The electrode 12 is disposed at a position facing the front and back surfaces of the steel strip 2 that moves in the electrolytic treatment tank 11. In this embodiment, when the electrode 12 facing the front surface of the steel strip 2 and the electrode 12 facing the back surface are used as a pair of electrodes, the electrode 12 is composed of a front half portion and a rear half portion of the electrolytic treatment tank 11 (of the steel strip 2). Two sets are provided on the upstream side and the downstream side in the transport direction.

支持ロール13は、前半部の一組の電極12と後半部の一組の電極12との間に配置されるロールである。支持ロール13は鋼帯2を挟持する二つのロールから構成され、この二つのロールにより、搬送中の鋼帯2がばたついたり弛んだりすることを抑える。   The support roll 13 is a roll disposed between the pair of electrodes 12 in the front half and the pair of electrodes 12 in the rear half. The support roll 13 is composed of two rolls that sandwich the steel strip 2, and the two rolls prevent the steel strip 2 being conveyed from flapping or loosening.

ダムロール14は、電解処理槽11に鋼帯2が入る入側の端、及び電解処理槽11から鋼帯が出る出側の端に配置される。ダムロール14は、それぞれ鋼帯2を挟持する二つのロールから構成され、このロールにより、電解質溶液3が電解処理槽11外に流出することを抑制する。   The dam roll 14 is disposed at the entrance end where the steel strip 2 enters the electrolytic treatment tank 11 and the exit end where the steel strip exits from the electrolytic treatment tank 11. The dam roll 14 is composed of two rolls each sandwiching the steel strip 2, and the roll prevents the electrolyte solution 3 from flowing out of the electrolytic treatment tank 11.

通電ロール15及びバックアップロール16は、これらを一組として、入側のダムロール14より上流側近傍、出側のダムロール14より下流側近傍に一組ずつ配置される。通電ロール15及びバックアップロール16は、鋼帯2を挟持することで、通電ロール15により鋼帯2の表面が負に帯電する。   The energizing roll 15 and the backup roll 16 are arranged in pairs near the upstream side of the incoming dam roll 14 and near the downstream side of the outgoing dam roll 14. The energizing roll 15 and the backup roll 16 sandwich the steel strip 2 so that the surface of the steel strip 2 is negatively charged by the energizing roll 15.

本実施形態において、水平型電気めっき設備1は、電解処理槽11が複数連なっている。この場合、上流側の電解処理槽11から出た鋼帯2は通電ロール15とバックアップロール16の間を通過して、下流側の電解処理槽11に搬送される。ここで、上記通電ロール15及びバックアップロール16は、上流側の電解処理槽11に着目すれば、出側に配置された通電ロール15及びバックアップロール16であり、下流側の電解処理槽11に着目すれば、入側に配置された通電ロール15及びバックアップロール16になる。このように、入側に配置されたものであるか、出側に配置されたものであるかは、着目する電解処理槽11により異なる。   In the present embodiment, the horizontal electroplating facility 1 includes a plurality of electrolytic treatment tanks 11. In this case, the steel strip 2 coming out of the upstream electrolytic treatment tank 11 passes between the energizing roll 15 and the backup roll 16 and is conveyed to the downstream electrolytic treatment tank 11. Here, the current-carrying roll 15 and the backup roll 16 are the current-carrying roll 15 and the backup roll 16 arranged on the outlet side when focusing on the upstream-side electrolytic treatment tank 11, and the downstream-side electrolytic treatment tank 11. If it does, it will become the electricity supply roll 15 and backup roll 16 which are arrange | positioned at the entrance side. Thus, whether it is arrange | positioned at the entrance side or what is arrange | positioned at the exit side changes with the electrolytic treatment tank 11 to which its attention is paid.

通電ロール研磨装置17は、通電ロール15の近傍に配置され、通電ロール15に付着した金属めっきを除去する。   The energizing roll polishing device 17 is disposed in the vicinity of the energizing roll 15 and removes metal plating attached to the energizing roll 15.

スプレー装置18は、通電ロール15の近傍に配置され、通電ロール15に水を散布する。   The spray device 18 is disposed in the vicinity of the energizing roll 15 and sprays water on the energizing roll 15.

図2は、スプレー装置18が通電ロール15に水4を散布する様子を示す模式図である。図2に示す通り、スプレー装置18は円筒状であり、円周面に9個の噴射孔を有する。   FIG. 2 is a schematic diagram showing a state in which the spray device 18 sprays the water 4 on the energizing roll 15. As shown in FIG. 2, the spray device 18 has a cylindrical shape and has nine injection holes on the circumferential surface.

スプレー装置が有する噴射孔の数は特に限定されず、通電ロール15の表面に全体的に水を散布できればよい。「全体的に」には、通電ロール15の表面に、噴射孔からの水が直接当たらない領域がある場合も含む。   The number of spray holes of the spray device is not particularly limited as long as water can be sprayed on the entire surface of the energizing roll 15. “Overall” includes the case where there is a region on the surface of the energizing roll 15 where the water from the spray holes does not directly hit.

また、スプレー装置18と通電ロール15の間の距離は、特に限定されず、所望の効果を奏するように適宜調整すればよい。所望の効果は水の水圧や、通電ロール15の表面における水が当たる領域の割合、水の流量(L/min)等を調整することで得られるため、上記距離も、水圧等を所望の範囲に調整する際に合わせて調整すればよい。なお、通常、通電ロール15表面に最も近い噴射孔の先端から、通電ロール15表面までの距離が20〜100cmの範囲で調整する。   Further, the distance between the spray device 18 and the energizing roll 15 is not particularly limited, and may be adjusted as appropriate so as to achieve a desired effect. Since the desired effect can be obtained by adjusting the water pressure, the ratio of the area where the surface of the energizing roll 15 is exposed to water, the flow rate of water (L / min), etc., the above-mentioned distance can also be adjusted within the desired range. It may be adjusted according to the adjustment. In general, the distance from the tip of the injection hole closest to the surface of the energizing roll 15 to the surface of the energizing roll 15 is adjusted in the range of 20 to 100 cm.

続いて、本発明の表面処理方法について説明する。本発明の表面処理方法は、水散布工程と、表面処理工程を有する。以下、各工程について説明する。   Then, the surface treatment method of this invention is demonstrated. The surface treatment method of the present invention includes a water spraying step and a surface treatment step. Hereinafter, each step will be described.

水散布工程とは、電解処理槽の入側及び/又は出側に配置された通電ロール上に水を散布する工程である。   A water spraying process is a process of spraying water on the energizing rolls arranged on the entry side and / or exit side of the electrolytic treatment tank.

図1に示す水平型電気めっき設備を用いる場合の、水散布工程とは、通電ロール15及びバックアップロール16の間に鋼帯2を通過させながら、通電ロール15の表面に対して、スプレー装置18により水を散布する工程である。   In the case of using the horizontal electroplating equipment shown in FIG. 1, the water spraying process is a spray device 18 on the surface of the energizing roll 15 while passing the steel strip 2 between the energizing roll 15 and the backup roll 16. Is a step of spraying water.

上記水散布工程において、上記鋼帯2は、それより上流の電解処理槽11で処理されている。このため、水散布工程で、通電ロール15及びバックアップロール16を通過する前の鋼帯2の表面には、その直前の電解処理槽11での表面処理により生じた生成物が付着している。   In the water spraying step, the steel strip 2 is treated in the electrolytic treatment tank 11 upstream thereof. For this reason, the product produced by the surface treatment in the electrolytic treatment tank 11 immediately before is attached to the surface of the steel strip 2 before passing through the energizing roll 15 and the backup roll 16 in the water spraying step.

上記生成物とは、金属および/または酸化物を指す。本発明の表面処理方法は、上記生成物が生じる可能性のある全ての表面処理の際に適用可能である。上記のような生成物は、通電ロールへの漏れ電流が大きくなる場合に、上記生成物が電析しやすくなることがあるという理由で、通電ロール15上に堆積しやすく、通電ロール15上に上記生成物が堆積すると通電不良の問題が発生する。   The product refers to a metal and / or an oxide. The surface treatment method of the present invention can be applied to all surface treatments where the above-mentioned product may be generated. The product as described above is likely to deposit on the energizing roll 15 because the product may be easily deposited when the leakage current to the energizing roll increases. When the product accumulates, a problem of poor conduction occurs.

本発明では、通電ロール15の表面に水を散布するため、上記生成物が通電ロール15上に堆積されそうになっても、水を散布することによって、コンダクターロール上の電解液が希釈され、Ni等が析出しにくくなることで、不純物の堆積が抑えられる。また、一時的に上記不純物が、通電ロール15上に存在する状態になっても、水の働きにより、上記生成物は通電ロール15からすぐに剥がれ落ちる傾向にある。なお、本実施形態においては、上記生成物は通電ロールから下へ落ち、めっき液循環タンクへ回収される仕組みになっている。   In the present invention, since water is sprayed on the surface of the energizing roll 15, even if the product is likely to be deposited on the energizing roll 15, by spraying water, the electrolyte on the conductor roll is diluted, By making it difficult for Ni or the like to precipitate, accumulation of impurities can be suppressed. Further, even when the impurities temporarily exist on the energizing roll 15, the product tends to peel off from the energizing roll 15 immediately due to the action of water. In the present embodiment, the product falls from the energizing roll and is collected in the plating solution circulation tank.

また、電解処理槽11で行われる電気めっきは、鋼帯2を陰極にして処理するため、処理中に酸化物が発生し、鋼帯2の表面に酸化物が付着しやすい。したがって、水散布工程で、通電ロール15及びバックアップロール16の間を通過する前の鋼帯2の表面には、その直前の電解処理槽11での表面処理により生じた酸化物が付着している。   Moreover, since the electroplating performed in the electrolytic treatment tank 11 is performed using the steel strip 2 as a cathode, an oxide is generated during the treatment, and the oxide tends to adhere to the surface of the steel strip 2. Therefore, the oxide produced by the surface treatment in the immediately preceding electrolytic treatment tank 11 is attached to the surface of the steel strip 2 before passing between the energizing roll 15 and the backup roll 16 in the water spraying step. .

水散布工程において、散布する「水」とは、HOを主成分とし、中性のものである。本発明において中性とはpHが6.5〜8.0の範囲にあるものを指す。 In the water spraying step, “water” to be sprayed is H 2 O as a main component and is neutral. In the present invention, neutral means that the pH is in the range of 6.5 to 8.0.

水散布工程において、スプレー装置18が散布する水の量は特に限定されないが、鋼帯2の表面に付着た水を回収したときに、回収された水中の電解質濃度が、電解処理槽11中の電解質濃度の1/2以下になるように、スプレー装置18が通電ロール15の表面に水を散布することが好ましい。スプレー装置18が散布する水の量が上記範囲にあることで、水で希釈して、上記生成物の生成量を最小化できるという効果がある。回収された水中の電解質濃度の下限は特に限定されないが、0.5L/min以上であることが好ましい。   In the water spraying step, the amount of water sprayed by the spray device 18 is not particularly limited, but when the water adhering to the surface of the steel strip 2 is recovered, the recovered electrolyte concentration in the electrolytic treatment tank 11 is It is preferable that the spray device 18 sprays water on the surface of the energizing roll 15 so that the electrolyte concentration is ½ or less. Since the amount of water sprayed by the spray device 18 is in the above range, there is an effect that the amount of product produced can be minimized by diluting with water. The lower limit of the electrolyte concentration in the recovered water is not particularly limited, but is preferably 0.5 L / min or more.

回収された水中の電解質濃度の測定において、鋼帯2の表面に付着した水の回収は、特に限定されないが、例えば、通電ロールの下に液の回収パンとバッファータンクを配置し、液をめっき液循環タンクへもどすルートを設ける方法が挙げられる。   In the measurement of the electrolyte concentration in the recovered water, the recovery of the water adhering to the surface of the steel strip 2 is not particularly limited. For example, a liquid recovery pan and a buffer tank are placed under the energizing roll, and the liquid is plated. There is a method of providing a route for returning to the liquid circulation tank.

散布される上記水の量に調整するためには、各噴射孔からの流量を0.5〜20L/minの範囲で調整することが好ましいが、流量をどの程度にするかは、通電ロールの表面積に対する水が当たる領域の比率や、全ノズルから単位時間当たりに散布される総水量等も考慮して決める必要がある。   In order to adjust the amount of water sprayed, it is preferable to adjust the flow rate from each injection hole in the range of 0.5 to 20 L / min. It is necessary to consider the ratio of the area where water hits the surface area, the total amount of water sprayed per unit time from all nozzles, and the like.

表面処理工程とは、金属帯を表面処理する工程を指す。上記の通り、不純物や酸化物が通電ロールに堆積して、通電不良を生じる可能性がある表面処理であっても、本発明は上記水散布工程を有するため、不純物や酸化物の通電ロールへの堆積が抑えられ、通電不良が発生しにくくなる。その結果、表面処理工程において、表面性状が良好である、表面処理が施された金属帯が得られる。   A surface treatment process refers to the process of surface-treating a metal strip. As described above, since the present invention includes the water spraying step even when the surface treatment has the possibility that impurities and oxides accumulate on the current-carrying roll and cause a current-carrying failure, to the current-carrying roll of impurities and oxides. Accumulation of electricity is suppressed, and it becomes difficult for electric conduction failure to occur. As a result, in the surface treatment step, a surface-treated metal strip having good surface properties can be obtained.

以下、実施例により、さらに具体的に本発明を説明する。なお、本発明は以下の実施例に限定されない。   Hereinafter, the present invention will be described more specifically with reference to examples. The present invention is not limited to the following examples.

発明例
第1図に示す設備を用いて以下の表面処理を行った。
Invention Example The following surface treatment was performed using the equipment shown in FIG.

ZnSO・7HOを155g/L、NiSO・6Hを23g/L、NaSOを55g/Lからなる電解質溶液(pH:1.2、50℃)を収容した電解処理槽において、68A/dmの陰極電流密度の条件でZn−Ni電気めっきを鋼帯に施した。Zn−Ni電気めっきのめっき組成はNi:12質量%、残部Znおよび不可避不純物であり、めっき付着量は片面あたり30g/m2である。そして、電解処理槽の端に配置されたダムロールから送り出された鋼帯を、次の通電ロールとバックアップロールの間に通すことで、通電ロールにより鋼帯を負に帯電させた。この際、スプレー装置から、通電ロールの表面に向けて、水(pH6.5〜8.0、水量2.5L/min)を散布した。なお、水量とは全ノズル(全噴射孔)から出る水の総量である。 Electrolytic treatment containing an electrolyte solution (pH: 1.2, 50 ° C.) composed of 155 g / L of ZnSO 4 .7H 2 O, 23 g / L of NiSO 4 .6H 2 O 3 and 55 g / L of Na 2 SO 4 in the bath, a Zn-Ni electroplating was applied to the steel strip under the conditions of cathode current density of 68A / dm 2. The plating composition of the Zn—Ni electroplating is Ni: 12% by mass, the balance Zn and unavoidable impurities, and the plating adhesion amount is 30 g / m 2 per side. And the steel strip sent out from the dam roll arrange | positioned at the edge of an electrolytic treatment tank was passed between the next electricity supply roll and the backup roll, and the steel belt was negatively charged with the electricity supply roll. At this time, water (pH 6.5 to 8.0, water amount 2.5 L / min) was sprayed from the spray device toward the surface of the energizing roll. The amount of water is the total amount of water coming out of all nozzles (all injection holes).

上記の処理において、鋼帯の表面に付着した水を回収したときに、回収された水中の電解質濃度が、電解処理槽中の電解質濃度の1/2以下になるように水量を調整して、スプレー装置から水を散布した。   In the above treatment, when the water adhering to the surface of the steel strip is collected, the amount of water is adjusted so that the electrolyte concentration in the collected water is 1/2 or less of the electrolyte concentration in the electrolytic treatment tank, Water was sprayed from the spray device.

また、実施例及び下記の比較例で使用したスプレー装置は、具体的には以下の通りである。塩化ビニル製、全長2000mm、直径22mmの筒状であり、直径18mmの噴射孔が18個設けられ、噴射孔間の間隔が100mmであるスプレー装置を用いた。7つのスプレー装置から7つの各通電ロールに水を散布できるように、水用のスプレー装置を配置した(実施例でのみ使用)。また、同様の形状のスプレー装置1つを希硫酸用として配置した(比較例でのみ使用)。また、通電ロール表面に最も近い噴射孔の先端から、通電ロール15表面までの距離が20〜100cmの範囲になるように調整した。なお、流量計はスプレー装置の端部に設けられ、この部分で流量を確認することで、所望の流量に調整可能である。   Moreover, the spray apparatus used by the Example and the following comparative example is specifically as follows. A spray device made of vinyl chloride, having a cylindrical shape with a total length of 2000 mm and a diameter of 22 mm, provided with 18 injection holes with a diameter of 18 mm, and an interval between the injection holes of 100 mm was used. The spray device for water was arrange | positioned so that water could be sprinkled from the seven spray devices to each of the seven energizing rolls (used only in the examples). Also, one spray device with the same shape was arranged for dilute sulfuric acid (used only in the comparative example). Moreover, it adjusted so that the distance from the front-end | tip of the injection hole nearest to the electricity supply roll surface to the electricity supply roll 15 surface might be in the range of 20-100 cm. In addition, a flow meter is provided in the edge part of a spray apparatus, and it can adjust to a desired flow volume by confirming a flow volume in this part.

上記処理を12時間連続で行ったところ、目視により、表面性状が良好である表面処理鋼帯が連続して得られることが確認された。   When the above treatment was carried out continuously for 12 hours, it was confirmed by visual observation that a surface-treated steel strip having a good surface property was obtained continuously.

ここで、表面性状が良好か否かは、目視により、以下の基準で評価した。
「○(良好)」:通電ロールの堆積物が鋼帯に転写しない場合
「×(不良)」:通電ロールの堆積物が鋼帯に転写する場合
比較例
水を20質量%の希硫酸を含む酸性溶液(pHが0.5〜1.5)に変更した以外は発明例と同様の方法で表面処理を行った。上記処理を12時間連続で行ったところ、目視により、表面性状が不良である表面処理鋼帯が得られることが確認された。なお、表面性状の評価方法は発明例の場合と同様である。
Here, whether or not the surface properties were good was evaluated by visual observation according to the following criteria.
“◯ (good)”: When the deposit on the current roll does not transfer to the steel strip “× (bad)”: When the deposit on the current roll transfers to the steel strip Comparative Example Water contains 20% by mass of dilute sulfuric acid Surface treatment was performed in the same manner as in the inventive examples except that the solution was changed to an acidic solution (pH 0.5 to 1.5). When the above treatment was performed continuously for 12 hours, it was confirmed by visual observation that a surface-treated steel strip having poor surface properties was obtained. The evaluation method of the surface property is the same as in the case of the inventive examples.

1 水平型電気めっき設備
11 電解処理槽
12 電極
13 支持ロール
14 ダムロール
15 通電ロール
16 バックアップロール
17 通電ロール研磨装置
18 スプレー装置
2 鋼帯
3 電解質溶液
DESCRIPTION OF SYMBOLS 1 Horizontal type electroplating equipment 11 Electrolytic processing tank 12 Electrode 13 Support roll 14 Dam roll 15 Current supply roll 16 Backup roll 17 Current supply roll polisher 18 Spray device 2 Steel strip 3 Electrolyte solution

Claims (2)

金属帯を搬送しながら表面処理する表面処理設備の電解処理槽の入側及び/又は出側に配置された通電ロール上に水を散布する水散布工程と、
金属帯を表面処理する表面処理工程を有する金属帯の表面処理方法。
A water spraying step of spraying water on energizing rolls arranged on the entry side and / or exit side of the electrolytic treatment tank of the surface treatment facility for carrying out the surface treatment while conveying the metal strip;
A surface treatment method for a metal strip, comprising a surface treatment step for surface-treating the metal strip.
前記水はpHが6.5〜8.0であり、
前記水散布工程は、金属帯の表面に付着した水を回収したときに、回収された水中の電解質濃度が、前記電解処理槽中の電解質濃度の1/2以下になるように、水を通電ロールに散布する工程である請求項1に記載の表面処理方法。
The water has a pH of 6.5 to 8.0,
In the water spraying step, when water adhering to the surface of the metal strip is collected, the water is energized so that the electrolyte concentration in the collected water is ½ or less of the electrolyte concentration in the electrolytic treatment tank. The surface treatment method according to claim 1, wherein the surface treatment method is a step of spraying on a roll.
JP2013056716A 2013-03-19 2013-03-19 Metal strip surface treatment method Active JP5821882B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2013056716A JP5821882B2 (en) 2013-03-19 2013-03-19 Metal strip surface treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2013056716A JP5821882B2 (en) 2013-03-19 2013-03-19 Metal strip surface treatment method

Publications (2)

Publication Number Publication Date
JP2014181382A true JP2014181382A (en) 2014-09-29
JP5821882B2 JP5821882B2 (en) 2015-11-24

Family

ID=51700395

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2013056716A Active JP5821882B2 (en) 2013-03-19 2013-03-19 Metal strip surface treatment method

Country Status (1)

Country Link
JP (1) JP5821882B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017115192A (en) * 2015-12-22 2017-06-29 Jfeスチール株式会社 Radial-cell type electroplating device and electroplated strip manufacturing method

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62284099A (en) * 1986-06-02 1987-12-09 Nippon Mining Co Ltd Conductive roll device
JPS63203793A (en) * 1987-02-17 1988-08-23 Kobe Steel Ltd Production of electroplated steel sheet
JPS63250492A (en) * 1987-04-07 1988-10-18 Sumitomo Metal Ind Ltd Electrodeposition preventing method for vertical plating equipment
JPH0417695A (en) * 1990-05-11 1992-01-22 Kawasaki Steel Corp Surface treatment method for metal strip
JPH05140797A (en) * 1991-11-18 1993-06-08 Sumitomo Metal Ind Ltd Production of continuously electroplated steel strip
JP2000096290A (en) * 1998-09-18 2000-04-04 Shinko Electric Ind Co Ltd Power feeder for long-sized belt-like body
JP2002030483A (en) * 2000-07-11 2002-01-31 Casio Micronics Co Ltd Chemical treating apparatus and chemical treating method using the same
US20060118424A1 (en) * 2002-06-17 2006-06-08 Toray Industries, Inc Method for Manufacturing plated film, cathode roll for plating, and method for manufacturing circuit board
JP2007016316A (en) * 2005-07-08 2007-01-25 Hoellmueller Maschinenbau Gmbh Apparatus and process for electrolytically treating of foils from roller to roller
JP2008248368A (en) * 2007-03-30 2008-10-16 Nikko Kinzoku Kk Method of recovering nickel from flush waste water after nickel strike plating

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62284099A (en) * 1986-06-02 1987-12-09 Nippon Mining Co Ltd Conductive roll device
JPS63203793A (en) * 1987-02-17 1988-08-23 Kobe Steel Ltd Production of electroplated steel sheet
JPS63250492A (en) * 1987-04-07 1988-10-18 Sumitomo Metal Ind Ltd Electrodeposition preventing method for vertical plating equipment
JPH0417695A (en) * 1990-05-11 1992-01-22 Kawasaki Steel Corp Surface treatment method for metal strip
JPH05140797A (en) * 1991-11-18 1993-06-08 Sumitomo Metal Ind Ltd Production of continuously electroplated steel strip
JP2000096290A (en) * 1998-09-18 2000-04-04 Shinko Electric Ind Co Ltd Power feeder for long-sized belt-like body
JP2002030483A (en) * 2000-07-11 2002-01-31 Casio Micronics Co Ltd Chemical treating apparatus and chemical treating method using the same
US20060118424A1 (en) * 2002-06-17 2006-06-08 Toray Industries, Inc Method for Manufacturing plated film, cathode roll for plating, and method for manufacturing circuit board
JP2007016316A (en) * 2005-07-08 2007-01-25 Hoellmueller Maschinenbau Gmbh Apparatus and process for electrolytically treating of foils from roller to roller
JP2008248368A (en) * 2007-03-30 2008-10-16 Nikko Kinzoku Kk Method of recovering nickel from flush waste water after nickel strike plating

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017115192A (en) * 2015-12-22 2017-06-29 Jfeスチール株式会社 Radial-cell type electroplating device and electroplated strip manufacturing method

Also Published As

Publication number Publication date
JP5821882B2 (en) 2015-11-24

Similar Documents

Publication Publication Date Title
JP7066707B2 (en) How to electroplat an uncoated steel strip with a plating layer
CN108624943A (en) A kind of horizontal continuity electroplanting device and preparation method thereof
JP5821882B2 (en) Metal strip surface treatment method
JP5212225B2 (en) Copper foil plating method and plating apparatus therefor
KR101690172B1 (en) Vertical continuous hot-dip galvanized plating bath and vertical type steel sheet coating device with the same
CN114174559A (en) Method and device for electrolytic coating of electrically conductive strips and/or fabrics using impulse technology
CN109312487B (en) Method and apparatus for manufacturing plated steel sheet
JP6414037B2 (en) Method for producing electroplating strip
KR101070976B1 (en) Method of attaching diamond using immersion plating, and apparatus for the method
JP6604342B2 (en) Electroplating method, electroplating equipment and method for producing electroplated steel sheet
JP7161146B2 (en) Zn-Ni alloy plated steel sheet manufacturing method and electroplating equipment
JP5084055B2 (en) Electrolytic degreasing apparatus and electrolytic degreasing method
JP6558418B2 (en) Electroplated steel sheet manufacturing method and electroplated steel sheet manufacturing apparatus
JP2007186755A (en) Method for producing tinned steel strip and tinned cell
JP4517177B2 (en) Treatment method of electroless nickel plating solution
JPH0352551B2 (en)
JP6988842B2 (en) Manufacturing method of electric Zn—Ni alloy plated steel sheet
JP2719030B2 (en) Metal band surface treatment method
JP2008248368A (en) Method of recovering nickel from flush waste water after nickel strike plating
JPH05106085A (en) Method for preventing elution of fe ion into electroplating solution
JPS586792B2 (en) Aenion no Metsukiyokuhenokiyoukiyuhouhou
JP2615226B2 (en) Method for removing fern-like patterns during electroplating of metal strip
TW585932B (en) Method of reducing defects caused by conductor roll surface anomalies using high volume bottom sprays
JPS63203793A (en) Production of electroplated steel sheet
JP3334579B2 (en) Method for producing galvanized steel sheet with excellent appearance

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20141027

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20150619

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150623

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150820

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20150908

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20150921

R150 Certificate of patent or registration of utility model

Ref document number: 5821882

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250