JP4581251B2 - Manufacturing method of steel sheet with good surface quality - Google Patents

Manufacturing method of steel sheet with good surface quality Download PDF

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JP4581251B2
JP4581251B2 JP2001010654A JP2001010654A JP4581251B2 JP 4581251 B2 JP4581251 B2 JP 4581251B2 JP 2001010654 A JP2001010654 A JP 2001010654A JP 2001010654 A JP2001010654 A JP 2001010654A JP 4581251 B2 JP4581251 B2 JP 4581251B2
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Prior art keywords
steel strip
water
annealing
surface quality
pure water
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JP2001010654A
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JP2002212643A (en
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直也 佐藤
恭裕 山田
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JFE Steel Corp
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JFE Steel Corp
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Description

【0001】
【発明の属する技術分野】
この発明は、良好な表面品質を有する鋼板の製造方法に係り、特に、冷間圧延鋼帯の焼鈍中に生成されるMn等の表面濃化物による表面品質の劣化を好適に防止するものに関する。
【0002】
【従来の技術】
近年、冷間圧延薄板を製造するにあたり、その焼鈍工程においてバッチ炉の代わりに連続焼鈍炉を用い、コイル状の材料(鋼帯)を炉の入口から連続的に炉内に送入して所定の熱処理を施す連続焼鈍法が、生産性の向上及び品質のばらつき減少のために採用されている。この場合、連続焼鈍炉内に機械的に送られながら再結晶過程を経て炉外に出た直後の鋼帯に対して、最終冷却が行われる。特に、ブリキ原板等を製造する際には、水冷により最終冷却を行うことで操業速度の高速化に対応した冷却能力向上を図っている。ここで、最終冷却では、浄水(工業用水)や軟水(CaやMgの含有量を少なくした水)を冷却水として使用している。
【0003】
そして、最近では、上記連続焼鈍装置の後に圧延機を直結して、焼鈍後の鋼帯を調質圧延もしくは二回目冷間圧延(以下、単に調質圧延という)する、すなわち軽い冷間加工を連続的に施すことにより、生産性及び歩留りの向上を図る方法が採用されている。例えば調質圧延されたブリキ原板にとって、板面の粗度,色調並びに形状は極めて重要な品質であり、これらの表面品質は焼鈍後の調質圧延によって殆ど決まるとされている。
【0004】
しかし、焼鈍時には、鋼中成分であるMn,Si,S等が鋼組織内を拡散して表面に集まり濃化物が生成される。これらMn等の濃化物は、調質圧延中のワークロールに堆積し、その堆積物が連続的に送られてくる鋼帯の板面に転写される。そのため、調質圧延後の鋼帯の表面の明度が低下し、色調,外観及び板面粗度等の表面品質が損なわれてしまうという問題点があった。
【0005】
また、Mn等の濃化物は焼鈍後に行われる水冷によりまだら状に剥離しやすく、調質圧延中のワークロールに不均一に堆積し、これが鋼帯板面に転写され、板幅方向の色調むら、いわゆるツートンカラーが発生するという問題もあった。
【0006】
【発明が解決しようとする課題】
本出願人は、Mn等の濃化物に起因する問題を解決するため、特許2938283 号の公報で記載されているように、冷間圧延鋼帯を、焼鈍後の最終冷却工程において濃度が重量%で0.01〜1 %の有機酸水溶液に浸漬して冷却しつつ、焼鈍時に鋼帯表面に生成したMn等の濃化物を除去し、その後連続的に調質圧延もしくは二回目冷間圧延する方法を開発した。この方法によると、焼鈍後の冷延圧延鋼帯を最終冷却工程において有機酸水溶液に浸漬して、焼鈍中に生成さたMn等の表面濃化物を均一に除去するものとしたから、次に続く調質圧延若しくは二回目冷間圧延後の鋼帯面での明度の低下、あるいはまだら状模様の発生がなく、製品の表面品質が保証される。
【0007】
しかし、上述した特許2938283 号の発明は、所定濃度の有機酸水溶液に設定するために、頻繁に濃度管理を行わなければならず、ランニングコストの面で問題があり、しかも、使用済みの有機酸水溶液を処理するための排水処理設備等も必要となるので、設備コストの面でも問題がある。
本発明は、上記事情に鑑みてなされたものであり、冷間圧延鋼帯の表面濃化物に起因する表面品質の問題を、ランニングコストや設備コストをかけず、比較的低コストで解決することができる表面品質の良好な鋼板の製造方法を提供することを目的としている。
【0008】
【課題を解決するための手段】
本発明者らは、従来、水冷により最終冷却を行っていた方法が、有機酸水溶液に浸漬する従来の方法と比較してランニングコストや設備コストの面で優れていることに着目した。ここで、従来の水冷による最終冷却では、浄水や軟水を冷却水として使用していたが、これら浄水や軟水は、不純物が多く含まれているので、鋼帯表面に生成したMn等の濃化物に対して反応性が低い。そこで、不純物が少なく、即ち、電気伝導度の低い冷却水を選択し、鋼帯表面に生成した濃化物に対して反応性を高くして均一に除去する方法について鋭意研究を重ねた。
【0009】
その結果、焼鈍後の鋼帯の最終冷却時の鋼帯温度を厳密に管理するとともに、電気伝導度が0.5 ×10-4Ω-1・m-1以下の純水に浸漬することにより、鋼帯を冷却しながら、同時にMn等の濃化物との反応により均一に除去できることを見出して本発明をなすに到った。
この方法によると、濃化物が調質圧延のワークロールに不均一に堆積することがなくなり、焼鈍後連続して調質圧延した際に鋼帯の表面粗度、色調が経時的に変化することがない。そのため、表面品質の良好な鋼板が安定して製造可能となる。また、純水を使用したことで、ランニングコストが殆ど掛からず、排水処理設備も不要となるので設備コストも低減することができる。
【0010】
ここで、前記純水に浸漬する直前の前記鋼帯の浸入温度は、120〜150℃に設定する。
すなわち、焼鈍後の鋼帯表面に生成したMn等の濃化物は、厚さが5〜10nm程度の原子レベルの堆積物であり、水槽に浸入する直前の高露点部で酸化による安定化が進むため、水に浸漬する直前の浸入板温は低くする必要があり、純水に浸漬する直前の鋼帯の浸入温度を150℃以下とする。一方、浸入板温が低くなり過ぎると反応性が低下し、また、操業速度も高速化できないため、鋼帯の浸入板温は120℃以上とする。
【0011】
したがって、本発明では、鋼帯の浸入温度を120〜150℃の低温度とし、濃化物を不安定状態として鋼帯の表面からの除去を容易とする。
【0012】
【発明の実施の形態】
以下、本発明の1実施形態を図面を参照して説明する。
図1は、本発明を実施する工程の概要を示したものである。ペイオフリール(POR)1の冷延コイルから巻戻された鋼帯2は、脱脂装置3を経て焼鈍炉4に搬送され焼鈍工程が行われる。その後直ちに、電気伝導度が0.5 ×10-4Ω-1・m-1以下の純水5Aを満たしている最終冷却用の水冷装置5に通され、浸漬されて冷却される。そして、水冷装置5を通過した鋼帯2は、ドライヤ6を経て調質圧延機7に送られて調質圧延され、テンションリール(TL)8で巻取られてブリキ原板製品が製造される。
【0013】
ここで、水冷装置5に浸漬する直前の鋼帯2(図1の符号Cで示す位置の鋼帯2)の温度は、120〜150℃に設定されている。
上記構成の工程によると、焼鈍炉4を通過した鋼帯2は、電気伝導度が0.5 ×10-4Ω-1・m-1以下の純水に浸漬したときに、鋼帯2の表面に生成されているMn等の濃化物が、不純物の少ない純水に対して反応性が高められて除去されやすくなる。そして、水冷装置5に浸漬する直前の鋼帯2の温度を120〜150℃に設定したことで、鋼帯2に生成されている濃化物は温度が低くなって不安定状態となり、鋼帯2の表面の濃化物の除去がさらに容易となる。
【0014】
また、水冷装置5に浸漬する直前の鋼帯2の温度を120〜150℃に設定したことから、ドライヤ6内に入る鋼帯2の温度が低くならず、ドライヤ6の乾燥効率の低下も防止することができる。
このため、本実施形態の工程は、濃化物が調質圧延機7のワークロールに不均一に堆積することがなく、調質圧延された際の鋼帯2の表面粗度、色調が経時的に変化することがないので、明度が高く表面品質の良好な鋼帯2が安定して製造可能となる。
【0015】
そして、本実施形態は、純水を使用したことで、ランニングコストが殆ど掛からず、従来のように排水処理設備も不要となるので、設備コストも低減することができる。しかも、本実施形態で使用した純水は、脱脂装置3で再利用することもできるという効果も奏する。
【0016】
【実施例】
本発明の工程(水冷装置5内に電気伝導度が0.5 ×10-4Ω-1・m-1以下の純水5Aを満たし、水冷装置5に浸漬する直前の鋼帯2の温度を120〜150℃に設定した工程)と、比較のために、水冷装置5内に浄水のみを満たしたものを用いる従来工程との2つの工程で、ブリキ原板を製造した。
【0017】
水冷装置5でMn等の濃化物の除去処理がなされた後、続いて調質圧延機7に送り込まれる直前の鋼帯2を、従来工程の場合と本発明の工程の場合とのそれぞれについてサンプリングし、Mn等の表面濃化状態をGDS(グロー放電発光分析装置)で測定し、図2(a)に従来工程の測定結果を、図2(b)に本発明の工程の測定結果を示す。なお、横軸は鋼板表面からの深さであり、縦軸は濃化物の量を表している。
【0018】
図2(a)の従来の工程と比較して、図2(b)の本発明の工程のものは、明らかにMn等の濃化物が除去されている。
また、従来の工程と本発明の工程において、調質圧延機7での圧延距離と製品ブリキ原板の色調(明度)との関係を測定した結果を図3にそれぞれ示した。これらの対比から、本発明の工程の方が、明度が高く、光沢性に優れることが明らかであり、本発明の工程では、色調むら、いわゆるツートンカラーの問題も発生しなかった。また、本発明の工程において、水冷装置5に浸漬する直前の鋼帯温度を、170℃とした場合についても、図3と同様の調査を行ったが、1.1程度の明度しか得られなかった。
【0019】
なお、本実施例はブリキ原板を対象としているが、本発明はブリキ原板のような表面処理用鋼板に限らず、その他、自動車用鋼板,一般冷延鋼板にも適用することができる。
【0020】
【発明の効果】
以上説明したように、本発明によれば、焼鈍炉を通過した鋼帯は、電気伝導度が0.5 ×10-4Ω-1・m-1以下の純水に浸漬したときに、鋼帯の表面に生成されているMn等の濃化物が、不純物の少ない純水に対して反応性が高められて除去されやすくなる。また、純水に浸漬する直前の鋼帯の温度を120〜150℃に設定したことで、鋼帯に生成されている濃化物は温度が低くなって不安定状態となるので、鋼帯の表面の濃化物の除去が促進される。したがって、調質圧延もしくは二回目冷間圧延後の鋼帯面の明度を高くでき、製品の表面品質が保証されるという効果を奏する。
【0021】
そして、本実施形態は、純水を使用したことで、ランニングコストが殆ど掛からず、従来のように排水処理設備も不要となるので、設備コストも低減することができる。
【図面の簡単な説明】
【図1】本発明の一実施例の製造工程の概要を示した図である。
【図2】調質圧延機に送り込まれる直前の鋼帯に生成した濃化物の状態をGDSで測定した結果を本発明と従来法とで示したグラフである。
【図3】一定距離調質圧延後の色調について本発明の方法と従来法とを比較して示したグラフである。
【符号の説明】
1 ペイオフリール(POR)
2 鋼帯
4 焼鈍炉
5 水冷装置
5A 純水
7 調質圧延機
8 テンションリール(TR)
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a steel sheet having good surface quality, and particularly to a method for suitably preventing deterioration of surface quality due to a surface concentrate such as Mn generated during annealing of a cold-rolled steel strip.
[0002]
[Prior art]
In recent years, when manufacturing cold-rolled thin sheets, a continuous annealing furnace is used instead of a batch furnace in the annealing process, and a coil-shaped material (steel strip) is continuously fed into the furnace from the furnace inlet to a predetermined temperature. The continuous annealing method in which the heat treatment is applied is employed for improving productivity and reducing quality variation. In this case, the final cooling is performed on the steel strip that has just been removed from the furnace through a recrystallization process while being mechanically fed into the continuous annealing furnace. In particular, when manufacturing a tin plate or the like, the cooling capacity is improved by responding to the increase in operation speed by performing final cooling by water cooling. Here, in the final cooling, purified water (industrial water) and soft water (water with reduced Ca and Mg contents) are used as cooling water.
[0003]
And recently, a rolling mill is directly connected after the continuous annealing apparatus, and the annealed steel strip is temper-rolled or second cold-rolled (hereinafter simply referred to as temper rolling), that is, light cold working is performed. A method of improving productivity and yield by applying continuously is adopted. For example, for a tin plate that has been temper-rolled, the roughness, color, and shape of the plate surface are extremely important qualities, and the surface quality is almost determined by the temper rolling after annealing.
[0004]
However, during annealing, Mn, Si, S, and the like, which are steel components, diffuse in the steel structure and collect on the surface to produce a concentrate. These concentrates such as Mn are deposited on the work rolls during temper rolling, and the deposits are transferred to the plate surface of the steel strip that is continuously fed. Therefore, the lightness of the surface of the steel strip after temper rolling is lowered, and there is a problem that the surface quality such as the color tone, the appearance, and the surface roughness is impaired.
[0005]
Concentrates such as Mn are easily peeled off by water cooling performed after annealing, and are unevenly deposited on the work roll during temper rolling, and this is transferred to the steel strip plate surface, resulting in uneven color tone in the plate width direction. There was also a problem that so-called two-tone color occurred.
[0006]
[Problems to be solved by the invention]
In order to solve the problem caused by the concentrate such as Mn, the applicant of the present invention has applied the cold-rolled steel strip to a concentration by weight in the final cooling step after annealing as described in Japanese Patent No. 2932883. While cooling by immersing in a 0.01% to 1% organic acid aqueous solution at the time of annealing, remove the concentrate such as Mn formed on the surface of the steel strip during annealing, and then perform temper rolling or second cold rolling continuously. developed. According to this method, the cold-rolled steel strip after annealing is immersed in an organic acid aqueous solution in the final cooling step to uniformly remove surface concentrates such as Mn generated during annealing. The surface quality of the product is assured with no decrease in lightness or mottled pattern on the steel strip after subsequent temper rolling or second cold rolling.
[0007]
However, the above-mentioned invention of Japanese Patent No. 2982883 has a problem in terms of running cost because it requires frequent concentration control in order to set an organic acid aqueous solution of a predetermined concentration, and the used organic acid has a problem. Since a waste water treatment facility for treating the aqueous solution is also required, there is a problem in terms of facility cost.
The present invention has been made in view of the above circumstances, and solves the problem of surface quality caused by the surface concentrate of a cold rolled steel strip at a relatively low cost without running costs and equipment costs. An object of the present invention is to provide a method for producing a steel sheet with good surface quality.
[0008]
[Means for Solving the Problems]
The inventors of the present invention focused on the fact that the method of performing the final cooling by water cooling is superior in terms of running cost and equipment cost as compared with the conventional method of immersing in an organic acid aqueous solution. Here, in the final cooling by conventional water cooling, purified water and soft water were used as cooling water, but these purified water and soft water contain a lot of impurities, so concentrates such as Mn generated on the surface of the steel strip. Is less reactive. Therefore, intensive research has been conducted on a method of selecting a cooling water with a small amount of impurities, that is, low electrical conductivity, and uniformly removing the concentrated product formed on the surface of the steel strip by increasing the reactivity.
[0009]
As a result, the steel strip temperature during final cooling of the steel strip after annealing is strictly controlled, and the steel strip is immersed in pure water with an electric conductivity of 0.5 × 10 -4 Ω -1 · m -1 or less. It was found that it can be uniformly removed by reaction with a concentrate such as Mn while cooling the band, and the present invention has been made.
According to this method, the concentrate does not accumulate unevenly on the work roll of temper rolling, and the surface roughness and color tone of the steel strip change over time when temper rolled continuously after annealing. There is no. Therefore, a steel plate having a good surface quality can be manufactured stably. In addition, since pure water is used, running costs are hardly required, and wastewater treatment equipment is not required, so that equipment costs can be reduced.
[0010]
Here, the intrusion temperature of the steel strip immediately before being immersed in the pure water is set to 120 to 150 ° C.
That is, the concentrate such as Mn formed on the surface of the steel strip after annealing is an atomic level deposit having a thickness of about 5 to 10 nm, and stabilization by oxidation proceeds at a high dew point immediately before entering the water tank. Therefore, it is necessary to lower the temperature of the infiltration plate immediately before being immersed in water, and the infiltration temperature of the steel strip immediately before being immersed in pure water is set to 150 ° C. or less. On the other hand, if the infiltration plate temperature becomes too low, the reactivity is lowered and the operation speed cannot be increased, so the infiltration plate temperature of the steel strip is set to 120 ° C. or higher.
[0011]
Therefore, in this invention, the penetration temperature of a steel strip is made into the low temperature of 120-150 degreeC, and the removal from the surface of a steel strip is made easy by making a concentrate into an unstable state.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
FIG. 1 shows an outline of a process for carrying out the present invention. The steel strip 2 unwound from the cold-rolled coil of the payoff reel (POR) 1 is conveyed to the annealing furnace 4 through the degreasing device 3, and an annealing process is performed. Immediately thereafter, it is passed through a final cooling water cooling device 5 filled with 5 A of pure water having an electric conductivity of 0.5 × 10 −4 Ω −1 · m −1 or less, and is immersed and cooled. And the steel strip 2 which passed the water-cooling apparatus 5 is sent to the temper rolling mill 7 through the dryer 6, temper-rolled, and is wound up with the tension reel (TL) 8, and a tinplate original plate product is manufactured.
[0013]
Here, the temperature of the steel strip 2 (the steel strip 2 at the position indicated by the symbol C in FIG. 1) immediately before being immersed in the water cooling device 5 is set to 120 to 150 ° C.
According to the process of the above configuration, when the steel strip 2 that has passed through the annealing furnace 4 is immersed in pure water having an electric conductivity of 0.5 × 10 −4 Ω −1 · m −1 or less, it is applied to the surface of the steel strip 2. The produced concentrate such as Mn is easily removed due to increased reactivity with pure water with few impurities. And by setting the temperature of the steel strip 2 just before being immersed in the water-cooling apparatus 5 to 120-150 degreeC, the concentrate produced | generated in the steel strip 2 becomes low temperature, becomes an unstable state, and the steel strip 2 It becomes easier to remove the concentrated product on the surface.
[0014]
Moreover, since the temperature of the steel strip 2 immediately before being immersed in the water cooling device 5 is set to 120 to 150 ° C., the temperature of the steel strip 2 entering the dryer 6 is not lowered, and the drying efficiency of the dryer 6 is prevented from being lowered. can do.
For this reason, in the process of the present embodiment, the concentrated product does not deposit non-uniformly on the work roll of the temper rolling mill 7, and the surface roughness and color tone of the steel strip 2 when temper rolled are time-dependent. Therefore, the steel strip 2 having high brightness and good surface quality can be manufactured stably.
[0015]
In this embodiment, since pure water is used, the running cost is hardly required, and the waste water treatment facility is not required as in the conventional case. Therefore, the facility cost can be reduced. And the pure water used by this embodiment also has the effect that it can also be reused with the degreasing apparatus 3. FIG.
[0016]
【Example】
The process of the present invention (the temperature of the steel strip 2 immediately before being immersed in the water cooling device 5 is filled with pure water 5A having an electric conductivity of 0.5 × 10 −4 Ω −1 · m −1 or less in the water cooling device 5). A tin plate was manufactured in two steps, a step set to 150 ° C.) and a conventional step using a water cooling device 5 in which only purified water was filled for comparison.
[0017]
After the removal of the concentrate such as Mn is performed by the water cooling device 5, the steel strip 2 immediately before being sent to the temper rolling mill 7 is sampled for each of the conventional process and the process of the present invention. Then, the surface concentration state of Mn or the like is measured by GDS (glow discharge emission spectrometer), FIG. 2 (a) shows the measurement result of the conventional process, and FIG. 2 (b) shows the measurement result of the process of the present invention. . The horizontal axis represents the depth from the steel sheet surface, and the vertical axis represents the amount of concentrate.
[0018]
Compared with the conventional process of FIG. 2A, the condensate such as Mn is clearly removed in the process of the present invention of FIG. 2B.
Moreover, the result of having measured the relationship between the rolling distance in the temper rolling mill 7 and the color tone (lightness) of the product tin plate in the conventional process and the process of the present invention is shown in FIG. From these contrasts, it is clear that the process of the present invention has higher brightness and superior glossiness, and the process of the present invention does not cause uneven color tone, so-called two-tone problems. Further, in the process of the present invention, even when the steel strip temperature just before dipping in the water cooling device 5 was set to 170 ° C., the same investigation as in FIG. 3 was performed, but only a lightness of about 1.1 was obtained. It was.
[0019]
In addition, although a present Example targets tinplate original plate, this invention is applicable not only to the steel plate for surface treatment like a tinplate original plate but to the steel plate for motor vehicles, and a general cold-rolled steel plate.
[0020]
【The invention's effect】
As described above, according to the present invention, when the steel strip that has passed through the annealing furnace is immersed in pure water having an electrical conductivity of 0.5 × 10 −4 Ω −1 · m −1 or less, Concentrates such as Mn generated on the surface are easily removed due to increased reactivity with pure water with few impurities. Moreover, since the temperature of the steel strip immediately before being immersed in pure water is set to 120 to 150 ° C., the concentrated product generated in the steel strip is lowered in temperature and becomes unstable. Removal of the concentrate is promoted. Therefore, the brightness of the steel strip surface after the temper rolling or the second cold rolling can be increased, and the surface quality of the product is guaranteed.
[0021]
In this embodiment, since pure water is used, the running cost is hardly required, and the waste water treatment facility is not required as in the conventional case. Therefore, the facility cost can be reduced.
[Brief description of the drawings]
FIG. 1 is a diagram showing an outline of a manufacturing process according to an embodiment of the present invention.
FIG. 2 is a graph showing the results of measuring the state of the concentrate formed on the steel strip immediately before being sent to the temper rolling mill by GDS, according to the present invention and the conventional method.
FIG. 3 is a graph showing a comparison between the method of the present invention and the conventional method with respect to the color tone after constant-distance temper rolling.
[Explanation of symbols]
1 Payoff reel (POR)
2 Steel strip 4 Annealing furnace 5 Water cooling device 5A Pure water 7 Temper rolling mill 8 Tension reel (TR)

Claims (1)

冷間圧延鋼帯を、焼鈍後の最終冷却工程において電気電導度が0.5×10−4Ω−1・m−1以下の純水に浸漬して冷却し、その際、前記純水に浸漬する直前の前記鋼帯の浸入温度を、当該鋼帯の表面に生成された濃化物と前記純水との反応性を高くする120〜150℃に設定し、その後、連続的に前記鋼帯を調質圧延若しくは二回目冷間圧延することを特徴とした表面品質の良好な鋼板の製造方法。The cold-rolled steel strip is cooled by immersing it in pure water having an electric conductivity of 0.5 × 10 −4 Ω −1 · m −1 or less in the final cooling step after annealing. The intrusion temperature of the steel strip immediately before dipping is set to 120 to 150 ° C. to increase the reactivity between the concentrated product generated on the surface of the steel strip and the pure water, and then continuously the steel strip. A method for producing a steel sheet with good surface quality, characterized in that temper rolling or second cold rolling is performed.
JP2001010654A 2001-01-18 2001-01-18 Manufacturing method of steel sheet with good surface quality Expired - Fee Related JP4581251B2 (en)

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CN104962704A (en) * 2015-06-13 2015-10-07 秦皇岛首秦金属材料有限公司 Heat treatment production method through air cooling after normalization
CN110052382A (en) * 2019-06-11 2019-07-26 鞍山发蓝股份公司 On-line cooling device after the japanning drying of steel belt for packages production line

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0234727A (en) * 1988-07-22 1990-02-05 Kawasaki Steel Corp Method and device for cooling metallic strip
JPH04293736A (en) * 1991-03-19 1992-10-19 Kawasaki Steel Corp Apparatus for dipping and cooling metal strip
JPH05339769A (en) * 1991-08-27 1993-12-21 Nobuo Sumida Pure water electrolytic cell provided with intermediate chamber

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0234727A (en) * 1988-07-22 1990-02-05 Kawasaki Steel Corp Method and device for cooling metallic strip
JPH04293736A (en) * 1991-03-19 1992-10-19 Kawasaki Steel Corp Apparatus for dipping and cooling metal strip
JPH05339769A (en) * 1991-08-27 1993-12-21 Nobuo Sumida Pure water electrolytic cell provided with intermediate chamber

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