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JPH0121240B2 - - Google Patents
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JPH0121240B2 - - Google Patents

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Publication number
JPH0121240B2
JPH0121240B2 JP59269368A JP26936884A JPH0121240B2 JP H0121240 B2 JPH0121240 B2 JP H0121240B2 JP 59269368 A JP59269368 A JP 59269368A JP 26936884 A JP26936884 A JP 26936884A JP H0121240 B2 JPH0121240 B2 JP H0121240B2
Authority
JP
Japan
Prior art keywords
tank
molten metal
plating
aqueous solution
acid aqueous
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.)
Expired
Application number
JP59269368A
Other languages
Japanese (ja)
Other versions
JPS61147900A (en
Inventor
Masahiko Ito
Heihachiro Midorikawa
Akira Minato
Teruo Yamaguchi
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP26936884A priority Critical patent/JPS61147900A/en
Publication of JPS61147900A publication Critical patent/JPS61147900A/en
Publication of JPH0121240B2 publication Critical patent/JPH0121240B2/ja
Granted legal-status Critical Current

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  • Heat Treatment Of Strip Materials And Filament Materials (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Electroplating Methods And Accessories (AREA)
  • Coating With Molten Metal (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔発明の利用分野〕 本発明は鋼板の連続めつき設備に係り、特に鋼
板の熱処理、鋼板表面の清浄化処理、活性化処理
を効率的に行い、また、選択的に電気めつき又は
溶融金属めつきを行うに好適な鋼板の連続めつき
設備に関する。 〔発明の背景〕 本発明による鋼板の連続めつきは亜鉛めつきに
限るものではないが、以下連続電気亜鉛めつきを
例にとつて従来技術を説明する。 従来、一般に鋼板の連続電気亜鉛めつきは、ア
ルカリ水溶液による脱脂、塩酸あるいは硫酸水溶
液による鋼板表示の活性化、硫酸亜鉛浴等でのめ
つきによる一連の湿式プロセスによつている。 電気めつき鋼板の性能には、めつき処理条件が
関与することは言うまでもないが、鋼板の脱脂清
浄、表面活性化などの前処理が大きく影響する。
前処理不良は特にめつき皮膜の均一性や密着性の
低下原因となり、これらはめつき本来の目的であ
る装飾性や耐食性を著しく損う。従つて完全な前
処理が必要である。 特開昭58−87295号に記載されているように、
従来、めつき前処理すなわち鋼板の脱脂清浄、表
面活性化処理は湿式法であつた。すなわち鋼板の
脱脂清浄化はアルカリ水溶液への浸漬あるいはそ
の吹付けにより行ない、これのみでは完全な脱脂
が難しいため、次いでアルカリ水溶液中で鋼板に
正または負の電圧を印加して電解脱脂をする。し
かる後に鋼板を水洗し、塩酸あるいは硫酸等の酸
水溶液に浸漬して表面の酸化物等を除去して活性
化し、水洗後、電気めつきをする。 しかし、この方法では水溶液中の湿式脱脂のた
め、処理速度が小さいと同時に、一旦アルカリ水
溶液中に溶出した油脂分が連続通板中に再び鋼板
に付着して再汚染する恐れがあるため十分な水洗
が必要となり、このため設備長さが大となり好し
くない。さらに電解脱脂ではアルカリ水溶液中に
鉄が溶出するため、これの除去処理が付随する。
これらの問題は水溶液中における湿式脱脂清浄処
理では必然的に生ずる。 また、電気めつきには通常冷延鋼板が用いられ
るが、この場合、上記従来の方法では鋼板の熱処
理は別ラインで行なう必要があり、これを同一ラ
インで連続処理できるようになつていないので生
産性等の面で効果的ではなかつた。また従来の連
続電気めつき設備は鋼板の溶融めつきにも兼用で
きるような構成上の配慮がされていなかつた。 〔発明の目的〕 本発明の目的は、鋼板の清浄及び活性化処理を
効率的に行ない且つ鋼板の熱処理と電気めつきの
一貫処理を行うことができ、また溶融金属めつき
にも選択的に兼用できる連続めつき設備を提供す
ることにある。 〔発明の概要〕 本発明の鋼帯の連続めつき設備は、鋼帯の入口
側から予熱炉、無酸化性雰囲気中で高温分解によ
る脱脂清浄処理を施す無酸化炉、還元性雰囲気中
で焼鈍熱処理を施す還元焼鈍炉、還元性雰囲気に
保つた冷却室、溶融金属めつき槽、冷却装置、鋼
帯に酸水溶液の液膜を塗布してその表面のスケー
ルを溶解する表面調整処理装置、水洗タンク、ド
ライヤー、スキンパスミル及びテンシヨンレベラ
からなる形状修正装置、酸洗タンクからなる表面
活性化装置、水洗タンク及び電気めつきタンクを
順次配置してなり、前記表面調整処理装置および
酸洗タンクはその中の酸水溶液を排出可能であ
り、前記電気めつきタンクはその中のめつき液を
排出可能であり、前記溶融金属めつき槽はその中
の溶融金属浴の注入・排出が自在であり、前記表
面調整処理装置及び酸洗タンクに酸水溶液を入
れ、前記電気めつきタンクにめつき液を入れ、且
つ前記溶融金属めつき槽から溶融金属浴を排出し
た状態において鋼帯を通板することによつて鋼帯
に連続電気めつきを施し、また、前記表面調整処
理装置および酸洗タンクから酸水溶液を排出し、
前記電気めつきタンクからめつき液を排出し、且
つ前記溶融金属めつき槽に溶融金属浴を注入した
状態において鋼帯を通板することによつて鋼帯に
連続溶融金属めつきを施す様に構成したことを特
徴とするものである。 〔発明の実施例〕 本発明においては、〔発明の背景〕で述べた従
来の湿式脱脂に伴う問題を解決し且つ同一ライン
で所要の熱処理を施すために、無酸化炉において
脱脂清浄処理を気相中で行なう。気相中での脱脂
清浄処理は、鋼板を高温に加熱し、付着している
油脂分を焼却することによつて簡便且つ大なる処
理速度で行うことができる。ここで鋼板表面は加
熱により酸化されてスケールが生成し、これはめ
つき膜の密着性を著しく阻害するので、続いて還
元焼鈍炉において水素と窒素ガスからなる還元雰
囲気の炉中で高温に保持してスケールを還元して
除去し、鋼板表面を活性な鉄面とする。この還元
雰囲気の炉内温度を変えることにより、鋼板に任
意の焼鈍熱処理を連続的に施すことができる。 上記気相脱脂処理および熱処理により鋼板は加
熱され、伸びによる板幅方向の反りなどの形状変
化が生じ、めつき処理に不都合を来たすので、テ
ンシヨンレベラ等により形状を修正し平担化す
る。しかし、高温で還元処理をした鋼板を形状修
正装置に供給する際に、高温の鋼板は大気中で酸
化されて表面にスケールが生成する。このスケー
ルは1μm以下の薄いものであるが、形状修正装置
のスキンパスミル及びテンシヨンレベラによる軽
圧延時に破壊され、破壊された微細スケールが鋼
板に押し込まれて表面損傷や特性劣化の原因とな
る。この問題は還元処理と形状修正処理の間に鋼
板のスケールを除去して形状修正に適した表面状
態にする表面調整処理工程を入れることにより解
決できる。スケール除去による表面調整処理は、
酸水溶液による化学的な溶解法で達せられる。 この表面調整処理のための化学的溶解法に用い
る酸水溶液としては塩酸、硫酸、リン酸等の無機
酸及びクエン酸、シユウ酸、酒石酸等の有機酸の
1種あるいは2種以上の混合が好都合であり、適
当濃度の水溶液として用いるのが良い。また、酸
水溶液には鋼板素地鉄の損失防止のためインヒビ
ターを添加するのが実用的である。添加インヒビ
ターは無機化合物よりも有機化合物が望しく、ア
ミン化合物、硫黄化合物、トリアゾール化合物な
どが実用的である。 この化学的溶解法による表面調整処理を行なう
には酸水溶液を満たした酸洗槽を設けて鋼板を連
続的に浸漬するのが最も簡便且つ実用的ではある
が、しかし、これは酸水溶液使用量が多く、装置
スペースも大となるので、本発明では酸洗槽への
浸漬以外の下記の手段によつて表面調整処理を行
なうのである。すなわち、前記の還元処理工程後
の鋼板温度は通常約450℃程度であり、大気中で
自然冷却及び強制風冷により30秒程度で約150℃
以下まで冷却される。しかるに鋼板の酸化は約
250℃以下の温度では極端に遅く、したがつてス
ケールの厚さはおおよそ450〜250℃に冷却される
までの間にほとんど決まり、鋼板の厚さにもよる
が、おおよそ1000〜3000Åと比較的薄い。このこ
とから本発明では、スケールの除去のために、鋼
板の酸洗槽への浸漬以外の効果的な手段として鋼
板表面へ酸水溶液の液膜を形成し、これによりス
ケールを溶解する手段を採用する。液膜の形成手
段としては第2図に例示するごとき、ロールコー
テイングは有効な手段である。すなわち第2図に
示すようにピツクアツプロール3により酸水溶液
2を持ち上げ、これに圧接するアプリケータロー
ル4上に酸水溶液の薄膜を形成し、アプリケータ
ロール4から鋼板1の表面に酸水溶液を転写し、
1000〜3000Å厚さのスケールを溶解する。ロール
は酸水溶液に浸食されないようにゴム巻きロール
が望しい。ゴム巻きロールを用いればロール表面
が柔軟であるため、鋼板の表面形状に追従でき
る。または、第3図に例示する如く、酸水溶液を
浸み込ませた軟いワイパー6により鋼板1の表面
に連続的に酸水溶液を塗布し、これにより薄いス
ケール層を溶解除去することもできる。ワイパー
材質は鋼板表面を傷つけず、しかも酸水溶液の保
持量が多いように多孔質でしかも弾力性の高いも
のが好しく、ガラス繊維あるいはスポンジなどが
使用できる。このようにロールコーターあるいは
ワイパーによる酸水溶液の液膜形成を利用すれば
装置をコンパクトに出来、しかも処理速度を大き
くできる利点がある。また酸水溶液の液膜形成
は、上記以外にも、酸水溶液の噴霧等によつても
達成することができる。なお、第2図および第3
図に示した表面調整処理装置は、その中の酸水溶
液を外部に拝除できるようになつている。 スケール溶解後の鋼板は水洗して残留酸水溶液
を除去し、乾燥後に次の形状修正装置へ送り、前
記した脱脂清浄処理および熱処理による鋼板の板
幅方向の反りなどの形状変化を修正する。形状修
正には、スキンパスミル及びテンシヨンレベラー
等による軽圧延や引張り伸びの付与により行なう
一般的な方法が用いられる。 形状修正後の鋼板は、電気めつきに適した表面
活性を付与するため、連続電気めつきの常套手段
である酸洗タンクで酸洗を行ない、水洗後に電気
めつき槽中で必要なめつき厚さに処理される。な
お、この酸洗タンク中の酸水溶液および電気めつ
き槽中のめつき液は排出可能である。 上述の一連の工程により、鋼板の脱脂清浄、熱
処理、スケール除去による表面調整、及び熱処理
時に生じた板反り等の形状変化の修正が同一ライ
ン内で効率的に一貫処理されるので、生産性良く
電気亜鉛めつき鋼板が製造される。 なお、本発明においては、脱脂清浄処理後の還
元焼鈍熱処理工程と表面調整処理工程との間には
溶融亜鉛めつき槽が設けられ、鋼帯はこの槽内を
通るようにする。この溶融亜鉛めつき槽はその中
に溶融亜鉛浴を注入したり又は空にしたりするこ
とができるようになつている。前述の電気メツキ
を行なう場合には、この溶融亜鉛槽は空にしてお
くのである。また、この槽内に溶融亜鉛浴を注入
し、且つ前記の表面調整処理装置中の酸水溶液お
よび酸洗タンク中の酸水溶液並びに電気めつき槽
中のめつき液を排出して本発明設備を運転すれ
ば、電気亜鉛めつき鋼帯の代わりに溶融亜鉛めつ
き鋼帯を製造し得る。 このように、本発明設備を用いれば、極めて容
易に同一めつきライン内で電気亜鉛めつき鋼板と
溶融亜鉛めつき鋼板を必要に応じて選択的に製造
し得るプロセスとすることができる。 なお、上記説明は鋼帯の亜鉛めつきを対象に述
べたが、本発明は必らずしも亜鉛めつき鋼板の製
造に限定されるものではなく、錫めつき等、一般
的なめつきに適用できるものである。 以下、本発明の実施例を具体的に説明する。 実施例 1 第1図には本発明に基づき鋼帯の連続電気亜鉛
めつきを行う設備の1例を示す。 第1図において、鋼帯1は、ペイオフリール、
カツテイングシヤー、ウエルダーなどの主な装置
から構成されている入側設備7により連続的に供
給され、次いで周囲大気から遮断され、雰囲気を
弱酸化性に調節された予熱炉8中に入る。予熱炉
8中で鋼帯1は約450℃程度まで加熱され、次い
で雰囲気を弱酸化性〜中性に保持した無酸化炉9
中で約700℃程度まで加熱され、鋼帯1の表面に
付着している冷間圧延油などが焼却され脱脂され
る。次に、鋼帯1は雰囲気をN2、H2の混合ガス
からなる還元性に保持した還元焼鈍炉10の中で
750〜800℃に加熱され、予熱炉8ないし無酸化炉
9中で生成したスケールを還元して清浄な鉄面を
得る。同時に鋼帯1は還元焼鈍炉10で必要な熱
処理を施される。次いで還元焼鈍炉10と同一の
雰囲気に保持された冷却室11の中で鋼帯1は約
450℃まで冷却され、溶融亜鉛を入れていない空
の溶融亜鉛めつき槽12を素通りして大気中に引
き出され、強制風冷装置13により150℃以下に
冷却される。次いで、第2図に示した表面調整処
理装置14に鋼帯1を導入し、前記約450〜150℃
に冷却される過程で生成したスケールを、5wt%
硫酸に1wt%ヘキサメチレンテトラミンを添加し
た酸水溶液を鋼帯1の両面に塗布することにより
溶解し、次いで水洗タンク15で残留する酸水溶
液を洗浄除去して、次工程の形状修正時の軽圧延
に適するように表面調整される。次いで鋼帯1
は、ドライヤー16で乾燥され、次いでスキンパ
スミル17、テンシヨンレベラー18からなる形
状修正装置により、脱脂清浄および熱処理時に生
じた板反りを修正し、平担化する。次いで鋼帯1
は酸洗タンク19内で10wt%の硫酸水溶液で表
面を活性化し、水洗タンク20で表面に残留する
酸水溶液を洗浄除去した後、電気亜鉛めつきタン
ク21内で硫酸亜鉛浴により電気亜鉛めつきを施
される。 第1表に本実施例で得られた電気亜鉛めつき鋼
板と、比較例として第1図の工程のうち表面調整
工程を含まない場合に得られた電気亜鉛めつき鋼
板の特性を示す。
[Field of Application of the Invention] The present invention relates to continuous plating equipment for steel plates, and in particular, it efficiently performs heat treatment of steel plates, cleaning treatment and activation treatment of steel plate surfaces, and selectively performs electroplating or molten metal plating. This invention relates to continuous plating equipment for steel sheets suitable for plating. [Background of the Invention] Although the continuous plating of steel sheets according to the present invention is not limited to galvanizing, the prior art will be described below using continuous electrogalvanizing as an example. Conventionally, continuous electrolytic galvanizing of steel sheets has generally been carried out by a series of wet processes including degreasing with an alkaline aqueous solution, activation of the steel plate markings with a hydrochloric acid or sulfuric acid aqueous solution, and plating in a zinc sulfate bath. It goes without saying that the performance of electroplated steel sheets is affected by the plating conditions, but pre-treatments such as degreasing, cleaning, and surface activation of the steel sheet also have a large effect.
Inadequate pretreatment particularly causes a decrease in the uniformity and adhesion of the plating film, which significantly impairs the decorative properties and corrosion resistance that are the original objectives of plating. Thorough pretreatment is therefore necessary. As described in Japanese Patent Application Laid-Open No. 58-87295,
Conventionally, pre-plating treatment, that is, degreasing, cleaning and surface activation treatment of steel sheets, has been performed using a wet method. That is, the steel plate is degreased and cleaned by dipping it in an alkaline aqueous solution or by spraying it.Since it is difficult to completely degrease with this alone, a positive or negative voltage is then applied to the steel plate in an alkaline aqueous solution to perform electrolytic degreasing. Thereafter, the steel plate is washed with water, immersed in an aqueous acid solution such as hydrochloric acid or sulfuric acid to remove oxides on the surface and activated, and after washing with water, electroplating is performed. However, since this method involves wet degreasing in an aqueous solution, the processing speed is slow, and at the same time, there is a risk that the oil and fats that have been eluted into the alkaline aqueous solution will re-adhere to the steel sheet during continuous sheet passing, resulting in re-contamination. This requires washing with water, which increases the length of the equipment, which is not preferable. Furthermore, since iron is eluted into the alkaline aqueous solution during electrolytic degreasing, a process for removing it is also required.
These problems inevitably occur in wet degreasing and cleaning treatment in an aqueous solution. Furthermore, cold-rolled steel sheets are usually used for electroplating, but in this case, the conventional method described above requires heat treatment of the steel sheets on a separate line, and it is not possible to perform continuous treatment on the same line. It was not effective in terms of productivity etc. Further, conventional continuous electroplating equipment has not been designed to be able to be used for hot-dipping of steel sheets. [Object of the Invention] The object of the present invention is to efficiently perform cleaning and activation treatment of a steel plate, and to perform an integrated process of heat treatment and electroplating of a steel plate, and to selectively also be used for molten metal plating. Our goal is to provide continuous plating equipment that can. [Summary of the Invention] The continuous plating equipment for steel strip of the present invention includes a preheating furnace, a non-oxidizing furnace that performs degreasing and cleaning treatment by high temperature decomposition in a non-oxidizing atmosphere, and annealing in a reducing atmosphere from the inlet side of the steel strip. A reduction annealing furnace for heat treatment, a cooling room maintained in a reducing atmosphere, a molten metal plating tank, a cooling device, a surface conditioning treatment device that applies a liquid film of acid aqueous solution to the steel strip to dissolve scale on its surface, and water washing. A shape correction device consisting of a tank, a dryer, a skin pass mill, and a tension leveler, a surface activation device consisting of a pickling tank, a water washing tank, and an electroplating tank are arranged in sequence, and the surface conditioning treatment device and pickling tank are The acid aqueous solution therein can be discharged, the electroplating tank can discharge the plating solution therein, and the molten metal plating tank can freely inject and discharge the molten metal bath therein. , the steel strip is passed through with an acid aqueous solution put into the surface conditioning treatment device and the pickling tank, a plating solution put into the electroplating tank, and a molten metal bath being discharged from the molten metal plating tank. performing continuous electroplating on the steel strip, and discharging the acid aqueous solution from the surface conditioning treatment device and the pickling tank;
Continuous molten metal plating is applied to the steel strip by discharging the plating solution from the electroplating tank and passing the steel strip with the molten metal bath injected into the molten metal plating tank. It is characterized by the following structure. [Embodiments of the Invention] In the present invention, in order to solve the problems associated with conventional wet degreasing described in [Background of the Invention] and to perform the required heat treatment on the same line, degreasing and cleaning treatment is carried out in a non-oxidizing furnace. Do it at the same time. Degreasing and cleaning treatment in the gas phase can be carried out simply and at a high processing speed by heating the steel plate to a high temperature and incinerating the fats and oils that have adhered to it. Here, the surface of the steel sheet is oxidized by heating and scale is generated, which significantly impedes the adhesion of the plating film, so the steel sheet is then kept at a high temperature in a reducing atmosphere consisting of hydrogen and nitrogen gas in a reduction annealing furnace. The scale is reduced and removed, and the steel plate surface becomes an active iron surface. By changing the furnace temperature of this reducing atmosphere, the steel plate can be continuously subjected to any desired annealing heat treatment. The steel sheet is heated by the above vapor phase degreasing treatment and heat treatment, and changes in shape such as warpage in the sheet width direction due to elongation occur, causing inconvenience in plating processing, so the shape is corrected and flattened using a tension leveler or the like. However, when a steel plate that has been subjected to reduction treatment at a high temperature is supplied to a shape modification device, the high-temperature steel plate is oxidized in the atmosphere and scale is generated on the surface. Although this scale is thin, less than 1 μm, it is destroyed during light rolling by the skin pass mill and tension leveler, which are shape modifying devices, and the destroyed fine scale is pushed into the steel plate, causing surface damage and property deterioration. This problem can be solved by inserting a surface conditioning treatment step between the reduction treatment and the shape modification treatment to remove scale from the steel plate and make the surface condition suitable for shape modification. Surface conditioning treatment by scale removal is
This is achieved by chemical dissolution using an acid aqueous solution. The acid aqueous solution used in the chemical dissolution method for this surface conditioning treatment is preferably one or a mixture of two or more of inorganic acids such as hydrochloric acid, sulfuric acid, and phosphoric acid, and organic acids such as citric acid, oxalic acid, and tartaric acid. Therefore, it is best to use it as an aqueous solution at an appropriate concentration. Further, it is practical to add an inhibitor to the acid aqueous solution in order to prevent loss of steel sheet base iron. The inhibitor to be added is preferably an organic compound rather than an inorganic compound, and amine compounds, sulfur compounds, triazole compounds, etc. are practical. In order to perform surface conditioning treatment using this chemical dissolution method, it is most convenient and practical to set up a pickling tank filled with an acid aqueous solution and continuously immerse the steel plate. Therefore, in the present invention, the surface conditioning treatment is performed by the following means other than immersion in a pickling bath. In other words, the temperature of the steel plate after the above-mentioned reduction treatment process is usually about 450°C, and it is reduced to about 150°C in about 30 seconds by natural cooling and forced air cooling in the atmosphere.
cooled down to below. However, the oxidation of steel plate is approximately
At temperatures below 250°C, it is extremely slow, so the thickness of the scale is almost determined by the time it is cooled to approximately 450-250°C, and it is relatively thin at approximately 1000-3000Å, depending on the thickness of the steel plate. thin. For this reason, in the present invention, in order to remove scale, an effective method other than dipping the steel plate in a pickling bath is to form a liquid film of an acid aqueous solution on the surface of the steel plate, thereby dissolving the scale. do. Roll coating, as illustrated in FIG. 2, is an effective means for forming a liquid film. That is, as shown in FIG. 2, the acid aqueous solution 2 is lifted up by the pick-up roll 3, a thin film of the acid aqueous solution is formed on the applicator roll 4 that is in pressure contact with this, and the acid aqueous solution is transferred from the applicator roll 4 to the surface of the steel plate 1. death,
Dissolve scales with a thickness of 1000-3000 Å. It is preferable that the roll be a rubber-wrapped roll so that it is not eroded by the acid aqueous solution. If a rubber-wrapped roll is used, the roll surface is flexible, so it can follow the surface shape of the steel plate. Alternatively, as illustrated in FIG. 3, the thin scale layer can be dissolved and removed by continuously applying the acid aqueous solution to the surface of the steel plate 1 using a soft wiper 6 impregnated with the acid aqueous solution. The wiper material is preferably porous and highly elastic so that it does not damage the surface of the steel plate and can retain a large amount of acid aqueous solution, and glass fiber or sponge can be used. In this way, the use of a roll coater or a wiper to form a liquid film of an aqueous acid solution has the advantage of making the apparatus more compact and increasing the processing speed. In addition to the above, the formation of a liquid film of the acid aqueous solution can also be achieved by spraying the acid aqueous solution or the like. In addition, Figures 2 and 3
The surface conditioning treatment device shown in the figure is designed to allow the acid aqueous solution contained therein to be expelled to the outside. After the scale has been dissolved, the steel plate is washed with water to remove residual acid aqueous solution, and after drying, it is sent to the next shape correction device to correct shape changes such as warping in the width direction of the steel plate due to the degreasing and cleaning treatment and heat treatment described above. For shape modification, general methods such as light rolling using a skin pass mill, tension leveler, etc., and applying tensile elongation are used. In order to impart surface activity suitable for electroplating, the steel sheet after shape modification is pickled in a pickling tank, which is a common method for continuous electroplating, and after washing with water, the required plating thickness is determined in the electroplating tank. will be processed. Note that the acid aqueous solution in the pickling tank and the plating solution in the electroplating tank can be discharged. Through the above-mentioned series of processes, the process of degreasing and cleaning the steel plate, heat treatment, surface conditioning by removing scale, and correction of shape changes such as plate warping that occur during heat treatment can be carried out efficiently and consistently on the same line, resulting in high productivity. Electrogalvanized steel sheets are manufactured. In the present invention, a hot-dip galvanizing tank is provided between the reduction annealing heat treatment step after the degreasing and cleaning treatment and the surface conditioning treatment step, and the steel strip passes through this tank. The hot-dip galvanizing tank is adapted to allow a hot-dip zinc bath to be filled or emptied into it. When carrying out the electroplating described above, this molten zinc bath is left empty. In addition, a molten zinc bath is poured into this tank, and the acid aqueous solution in the surface conditioning treatment device, the acid aqueous solution in the pickling tank, and the plating solution in the electroplating tank are discharged to operate the equipment of the present invention. In operation, hot-dip galvanized steel strip can be produced instead of electrogalvanized steel strip. As described above, by using the equipment of the present invention, it is possible to achieve a process in which electrogalvanized steel sheets and hot-dip galvanized steel sheets can be selectively manufactured as necessary within the same plating line very easily. Although the above explanation has been made with reference to galvanizing steel strips, the present invention is not necessarily limited to the production of galvanized steel sheets, and can be applied to general plating such as tin plating. It is applicable. Examples of the present invention will be specifically described below. Example 1 FIG. 1 shows an example of equipment for continuous electrogalvanizing of steel strips according to the present invention. In FIG. 1, the steel strip 1 is a payoff reel,
It is continuously supplied by an inlet equipment 7 consisting of main equipment such as a cutting shear and a welder, and then enters a preheating furnace 8 which is isolated from the surrounding atmosphere and whose atmosphere is adjusted to be slightly oxidizing. The steel strip 1 is heated to about 450°C in a preheating furnace 8, and then transferred to a non-oxidizing furnace 9 in which the atmosphere is maintained at a weakly oxidizing to neutral atmosphere.
Inside, the steel strip 1 is heated to about 700°C, and cold rolling oil and the like adhering to the surface of the steel strip 1 are incinerated and degreased. Next, the steel strip 1 is placed in a reduction annealing furnace 10 in which the atmosphere is maintained in a reducing atmosphere consisting of a mixed gas of N 2 and H 2 .
It is heated to 750 to 800°C, and the scale generated in the preheating furnace 8 to the non-oxidation furnace 9 is reduced to obtain a clean iron surface. At the same time, the steel strip 1 is subjected to necessary heat treatment in the reduction annealing furnace 10. Next, the steel strip 1 is heated in a cooling chamber 11 maintained in the same atmosphere as the reduction annealing furnace 10.
It is cooled to 450°C, passed through an empty hot-dip galvanizing tank 12 containing no molten zinc, and drawn out into the atmosphere, where it is cooled to below 150°C by a forced air cooling device 13. Next, the steel strip 1 is introduced into the surface conditioning treatment device 14 shown in FIG.
The scale generated during the cooling process is reduced to 5wt%.
An acid aqueous solution prepared by adding 1wt% hexamethylenetetramine to sulfuric acid is applied to both sides of the steel strip 1 to dissolve it, and then the remaining acid aqueous solution is washed away in a water washing tank 15 and used for light rolling during shape correction in the next process. The surface is adjusted to suit. Then steel strip 1
is dried in a dryer 16, and then a shape correcting device consisting of a skin pass mill 17 and a tension leveler 18 corrects the warping of the plate caused during degreasing, cleaning and heat treatment, and flattens it. Then steel strip 1
The surface is activated with a 10wt% sulfuric acid aqueous solution in the pickling tank 19, and the acid aqueous solution remaining on the surface is washed away in the water washing tank 20, and then electrogalvanized with a zinc sulfate bath in the electrogalvanizing tank 21. will be administered. Table 1 shows the characteristics of the electrogalvanized steel sheet obtained in this example and the electrogalvanized steel sheet obtained as a comparative example in the process shown in FIG. 1, which did not include the surface conditioning step.

【表】 実施例 2 実施例1と同じ処理工程で、表面調整処理装置
14として第3図に示したものを用いて、電気亜
鉛めつき鋼板を製造した。表面調整処理装置14
では鋼帯1の表面に10wt%塩酸に1wt%ヘキサメ
チレンテトラミンを添加した酸水溶液を塗布して
スケールを除去した。実施例1の場合と同様に、
得られた電気亜鉛めつき鋼板の特性は極めて満足
すべきものであつた。 実施例 3 第1図に示した練続亜鉛めつき設備において、
溶融亜鉛めつき槽12に450℃の溶融亜鉛浴を満
たし、表面調整処理装置14内の酸水溶液及び酸
洗タンク19内の酸水溶液を取り除き、さらに電
気亜鉛めつきタンク21内の硫酸亜鉛めつき液を
抜いて空にし、実施例1と同様に鋼帯1を連続通
板することにより美麗な溶融亜鉛めつき鋼板を得
た。 〔発明の効果〕 本発明の連続めつき設備においては、無酸化炉
にて無酸化性雰囲気中で油脂類を高温分解させる
ので、鋼板表面の酸化を促進させることなく、脱
脂処理ができる。さらに次の工程である還元焼鈍
炉では、還元性雰囲気中で焼鈍熱処理するため、
冷延鋼帯表面の初期に生成した極めて薄い酸化層
のみを還元すればよいので、炉の温度を必要以上
に高くすることなく鋼種に応じた焼鈍温度とする
ことができ、したがつて鋼帯の必要以上の軟化を
防ぐことができる。さらに、電気めつき前の表面
活性化を行なう酸洗では、スケールが既に除去さ
れているため、極めて短時間の酸洗処理で十分で
あるので、酸洗工程の処理時間を一般の電気めつ
き設備におけるよりも遥かに短時間で行なえるた
め、電気めつき設備の高速化ができる。また同一
ライン内で鋼帯の脱脂清浄処理および熱処理と、
めつき処理とを行なうことができるので、生産性
が向上する。 しかも、本発明においては、還元焼鈍炉での熱
処理後、電気めつき処理前に、該熱処理に因る鋼
帯の形状変化を修正するに適した表面調整処理を
行なうので、表面欠陥のない美麗な電気めつき鋼
板が得られる。しかも、本発明の設備配置によれ
ば、この表面調整処理は比較的薄いスケールを溶
解除去すればよいので、酸洗槽への浸漬などの如
き大型の装置でなくて、酸水溶液の膜を鋼帯に塗
布してその表面のスケールを溶解するというコン
パクトな表面調整処理装置で足りる利点がある。 さらに本発明の鋼帯連続めつき設備によれば、
表面調整処理装置の前に、溶融金属浴の注入・排
出の自在な溶融めつき槽を配置したことによつ
て、電気めつきと溶融金属めつきを同一ラインで
使い分けることが出来、薄めつきの需要には電気
めつきを、厚めつきの需要には溶融金属めつきと
いう具合に、随時、目的に応じためつき鋼板の製
造が経済的に出来る利点がある。しかも、電気め
つきは、めつき液(水溶液)をめつき槽に入れ替
えるだけで、極めて簡単に種々のめつき鋼板を得
ることができ、多目的めつき鋼板が得られるとい
う特徴があり、一方、溶融金属めつきは、或る限
られた種類の金属しかできないが、大量生産に極
めて有利であり、少品種多量生産に適するという
特徴があるところ、本発明の連続めつき設備はこ
の両者の特徴を同一ラインで使い分けることがで
き、工業上極めて大きい効果を有する。
[Table] Example 2 An electrogalvanized steel sheet was manufactured in the same process as in Example 1 using the surface conditioning treatment apparatus 14 shown in FIG. 3. Surface conditioning treatment device 14
Then, an acid aqueous solution prepared by adding 1 wt % hexamethylenetetramine to 10 wt % hydrochloric acid was applied to the surface of the steel strip 1 to remove scale. As in Example 1,
The properties of the electrogalvanized steel sheet obtained were extremely satisfactory. Example 3 In the continuous galvanizing equipment shown in Fig. 1,
The hot-dip galvanizing tank 12 is filled with a 450°C molten zinc bath, the acid aqueous solution in the surface conditioning treatment device 14 and the acid aqueous solution in the pickling tank 19 are removed, and then the electrolytic galvanizing tank 21 is coated with zinc sulfate. The liquid was drained and emptied, and the steel strip 1 was continuously passed in the same manner as in Example 1 to obtain a beautiful hot-dip galvanized steel sheet. [Effects of the Invention] In the continuous plating equipment of the present invention, since fats and oils are decomposed at high temperature in a non-oxidizing atmosphere in a non-oxidizing furnace, degreasing can be performed without promoting oxidation of the steel sheet surface. Furthermore, in the next step, the reduction annealing furnace, annealing heat treatment is performed in a reducing atmosphere.
Since it is necessary to reduce only the extremely thin oxide layer formed on the surface of the cold-rolled steel strip, the annealing temperature can be adjusted to suit the steel type without raising the furnace temperature unnecessarily. Unnecessary softening of the material can be prevented. Furthermore, in pickling to activate the surface before electroplating, since scale has already been removed, an extremely short pickling time is sufficient. Since it can be done in a much shorter time than it would take to use electroplating equipment, it is possible to speed up electroplating equipment. In addition, degreasing, cleaning and heat treatment of steel strips are carried out on the same line.
Since plating processing can be performed, productivity is improved. Moreover, in the present invention, after the heat treatment in the reduction annealing furnace and before the electroplating treatment, a surface conditioning treatment suitable for correcting the change in shape of the steel strip due to the heat treatment is performed, so that the steel strip has a beautiful surface without any defects. An electroplated steel sheet can be obtained. Moreover, according to the equipment arrangement of the present invention, this surface conditioning treatment only requires dissolving and removing relatively thin scale, so it is not necessary to use large equipment such as immersion in a pickling tank, and to apply a film of acid aqueous solution to the steel. It has the advantage that a compact surface conditioning treatment device that applies it to the strip and dissolves scale on its surface is sufficient. Furthermore, according to the steel strip continuous plating equipment of the present invention,
By placing a molten metal plating tank in front of the surface conditioning treatment equipment, where the molten metal bath can be freely injected and discharged, electroplating and molten metal plating can be used on the same line, meeting the demand for thinner plating. It has the advantage that it is possible to economically manufacture tempered steel sheets depending on the purpose, such as electroplating for the needs of thicker plates and molten metal plating for the needs of thicker plates. In addition, electroplating has the feature that it is possible to obtain various types of plated steel sheets extremely easily by simply replacing the plating solution (aqueous solution) in the plating tank, and that multi-purpose plated steel sheets can be obtained. Although molten metal plating can only be applied to certain limited types of metals, it is extremely advantageous for mass production and is suitable for mass production of small numbers of products.The continuous plating equipment of the present invention has the characteristics of both. can be used separately on the same line, which has an extremely large industrial effect.

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

第1図は本発明の一実施例のめつき工程を示す
図、第2図、第3図は本発明に用いる表面調整処
理装置の一実施例を示す図である。 1……鋼帯、2……酸水溶液、3……ピツクア
ツプロール、4……アプリケータロール、6……
ワイパー、7……入側設備、8……予熱炉、9…
…無酸化炉、10……還元焼鈍炉、11……冷却
室、12……溶融めつき槽、13……強制風冷装
置、14……表面調整処理装置、15……水洗タ
ンク、16……ドライヤー、17……スキンパス
ミル、18……テンシヨンレベラー、19……酸
洗タンク、20……水洗タンク、21……電気亜
鉛めつきタンク。
FIG. 1 is a diagram showing a plating process according to an embodiment of the present invention, and FIGS. 2 and 3 are diagrams showing an embodiment of a surface conditioning treatment apparatus used in the present invention. 1... Steel strip, 2... Aqueous acid solution, 3... Pick-up roll, 4... Applicator roll, 6...
Wiper, 7...Inlet equipment, 8...Preheating furnace, 9...
... Non-oxidation furnace, 10 ... Reduction annealing furnace, 11 ... Cooling room, 12 ... Melt plating tank, 13 ... Forced air cooling device, 14 ... Surface conditioning treatment device, 15 ... Water washing tank, 16 ... ... Dryer, 17 ... Skin pass mill, 18 ... Tension leveler, 19 ... Pickling tank, 20 ... Water washing tank, 21 ... Electrogalvanizing tank.

Claims (1)

【特許請求の範囲】[Claims] 1 鋼帯の入口側から予熱炉、無酸化性雰囲気中
で高温分解による脱脂清浄処理を施す無酸化炉、
還元性雰囲気中で焼鈍熱処理を施す還元焼鈍炉、
還元性雰囲気に保つた冷却室、溶融金属めつき
槽、冷却装置、鋼帯に酸水溶液の液膜を塗布して
その表面のスケールを溶解する表面調整処理装
置、水洗タンク、ドライヤー、スキンパスミル及
びテンシヨンレベラからなる形状修正装置、酸洗
タンクからなる表面活性化装置、水洗タンク及び
電気めつきタンクを順次配置してなり、前記表面
調整処理装置および酸洗タンクはその中の酸水溶
液を排出可能であり、前記電気めつきタンクはそ
の中のめつき液を排出可能であり、前記溶融金属
めつき槽はその中の溶融金属浴の注入・排出が自
在であり、前記表面調整処理装置及び酸洗タンク
に酸水溶液を入れ、前記電気めつきタンクにめつ
き液を入れ、且つ前記溶融金属めつき槽から溶融
金属浴を排出した状態において鋼帯を通板するこ
とによつて鋼帯に連続電気めつきを施し、また、
前記表面調整処理装置および酸洗タンクから酸水
溶液を排出し、前記電気めつきタンクからめつき
液を排出し、且つ前記溶融金属めつき槽に溶融金
属浴を注入した状態において鋼帯を通板すること
によつて鋼帯に連続溶融金属めつきを施す様に構
成したことを特徴とする鋼帯の連続めつき設備。
1. A preheating furnace from the inlet side of the steel strip, a non-oxidizing furnace that performs degreasing and cleaning treatment by high temperature decomposition in a non-oxidizing atmosphere,
A reduction annealing furnace that performs annealing heat treatment in a reducing atmosphere;
A cooling room maintained in a reducing atmosphere, a molten metal plating tank, a cooling device, a surface conditioning treatment device that applies a liquid film of acid aqueous solution to the steel strip to dissolve scale on its surface, a water washing tank, a dryer, a skin pass mill, and A shape correction device consisting of a tension leveler, a surface activation device consisting of a pickling tank, a water washing tank, and an electroplating tank are arranged in sequence, and the surface conditioning treatment device and the pickling tank discharge the acid aqueous solution therein. The electroplating tank is capable of discharging the plating liquid therein, the molten metal plating tank is capable of freely injecting and discharging the molten metal bath therein, and the surface conditioning treatment device and A steel strip is formed by pouring an acid aqueous solution into a pickling tank, pouring a plating solution into the electroplating tank, and passing the steel strip in a state in which the molten metal bath is discharged from the molten metal plating tank. Continuous electroplating is applied, and
The acid aqueous solution is discharged from the surface conditioning treatment device and the pickling tank, the plating solution is discharged from the electroplating tank, and the molten metal bath is poured into the molten metal plating tank, and then the steel strip is passed through. 1. Continuous plating equipment for steel strips, characterized in that the equipment is configured to continuously apply molten metal plating to steel strips.
JP26936884A 1984-12-20 1984-12-20 Continuous plating equipment for steel strips Granted JPS61147900A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26936884A JPS61147900A (en) 1984-12-20 1984-12-20 Continuous plating equipment for steel strips

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26936884A JPS61147900A (en) 1984-12-20 1984-12-20 Continuous plating equipment for steel strips

Publications (2)

Publication Number Publication Date
JPS61147900A JPS61147900A (en) 1986-07-05
JPH0121240B2 true JPH0121240B2 (en) 1989-04-20

Family

ID=17471413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26936884A Granted JPS61147900A (en) 1984-12-20 1984-12-20 Continuous plating equipment for steel strips

Country Status (1)

Country Link
JP (1) JPS61147900A (en)

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JPS5919195B2 (en) * 1979-01-06 1984-05-02 中外炉工業株式会社 Method and device for cleaning treated materials such as oil-stained steel parts

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010116593A (en) * 2008-11-12 2010-05-27 Kobe Steel Ltd Method for manufacturing high-strength hot-dip galvannealed steel sheet, and high-strength hot-dip galvannealed steel sheet

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JPS61147900A (en) 1986-07-05

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