JPH0379795A - Method and apparatus for continuously annealing and pickling stainless steel strip - Google Patents

Method and apparatus for continuously annealing and pickling stainless steel strip

Info

Publication number
JPH0379795A
JPH0379795A JP21506989A JP21506989A JPH0379795A JP H0379795 A JPH0379795 A JP H0379795A JP 21506989 A JP21506989 A JP 21506989A JP 21506989 A JP21506989 A JP 21506989A JP H0379795 A JPH0379795 A JP H0379795A
Authority
JP
Japan
Prior art keywords
pickling
stainless steel
zone
steel strip
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.)
Pending
Application number
JP21506989A
Other languages
Japanese (ja)
Inventor
Hideki Emoto
江本 秀樹
Takeo Onishi
大西 建男
Masanobu Ochiai
落合 政信
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
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP21506989A priority Critical patent/JPH0379795A/en
Publication of JPH0379795A publication Critical patent/JPH0379795A/en
Pending legal-status Critical Current

Links

Landscapes

  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Abstract

PURPOSE:To continuously anneal and pickle a stainless steel strip with superior productivity in small facilities by carrying out annealing by indirect heating in a reducing atmosphere and subsequent pickling by electrolytic pickling with a nitric acid-hydrofluoric acid soln. as an electrolytic soln. CONSTITUTION:A stainless steel strip S is introduced into a vertical annealing furnace filled with a reducing atmosphere, e.g. composed of 3-15% gaseous H2 and the balance gaseous N2. In the furnace, the strip S is indirectly heated with radiant tubes, etc., by passing through a preheating zone 1, a heating zone 2 and a soaking zone 3 and the heated strip S is passed through a cooling zone 4 and cooled to ordinary temp. with a final cooler 5. The strip S is then immersed in an aq. sulfuric acid soln. having 20% concn. at 70 deg.C in a vessel 6 for about 10sec and electrolytic pickling is carried out by passing through a vessel 7 contg. an electrolytic soln. contg. 20% nitric acid and 5-15% hydrofluoric acid. The strip S is further passed through a washing vessel 8 and a drier 9. A stainless steel strip free from oxide scale on the surface is efficiently produced in small facilities.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 この発明は、ステンレス鋼帯の連続lA鈍・酸洗方法及
びその設備に関し、特にステンレス鋼帯の連続焼鈍・酸
洗処理能力の有利な向上を、処理ラインの効果的な短縮
化に併せ、実現しようとするものである。
[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a continuous lA annealing/pickling method for stainless steel strips and its equipment, and particularly to an advantageous improvement in the continuous annealing/pickling processing ability of stainless steel strips. The aim is to achieve this by effectively shortening the processing line.

〈従来の技術〉 冷間圧延後のステンレスt14’4Fは、一般に連続焼
鈍・酸洗設#(^nealing and Ptckl
ing Line : APL)によって連続的な焼鈍
酸洗処理が施される。
<Prior art> Stainless steel T14'4F after cold rolling is generally subjected to continuous annealing and pickling.
Continuous annealing and pickling treatment is carried out by the ing line (APL).

ステンレス鋼帯の連続焼鈍においては、5US304の
如きオーステナイト系で1010〜1150°Cと非常
に高温にしなければならないため、生産性や保全性など
の点から、加熱手段として、普通鋼の場合に一般に使用
されている間接加熱タイプではなく、直火式が採用され
ている。
Continuous annealing of stainless steel strips requires extremely high temperatures of 1010 to 1150°C for austenitic steel such as 5US304, so from the viewpoint of productivity and maintainability, the heating means is generally not used for ordinary steel. Instead of the indirect heating type used, a direct flame type is used.

しかしながら、かかる直火式の加熱方式では、鋼帯表面
に酸化皮膜が生成するため、焼鈍後、酸洗による脱スケ
ールが不可欠である。
However, in such a direct heating method, an oxide film is formed on the surface of the steel strip, so descaling by pickling is essential after annealing.

ステンレス鋼の生成する酸化皮膜は、臂通鋼のそれと比
べるとはるかに緻密、強固であり、しかもかかる緻密化
傾向は、炉内0□濃度が零に近づくほど高まることから
、従来は、後段の酸洗工程における脱スケール処理を容
易にするため、炉内雰囲気はO1濃度:2〜3%程度の
酸化性雰囲気とされていた。
The oxide film formed on stainless steel is much denser and stronger than that on Ootsuki steel, and this tendency to densify increases as the 0□ concentration in the furnace approaches zero. In order to facilitate the descaling process in the pickling process, the atmosphere in the furnace was an oxidizing atmosphere with an O1 concentration of about 2 to 3%.

従って、スケール生成量が多く、この酸化スケールがハ
ースロールに付着、更に成長してステンレス鋼帯にいわ
ゆるピックアップ疵を発生させる。
Therefore, a large amount of scale is produced, and this oxidized scale adheres to the hearth roll and further grows, causing so-called pickup flaws in the stainless steel strip.

このピックアップ疵を防止するために、ハースロールを
アスベスト製ロールとし、しかもロール本数を極力少な
くしてステンレス鋼帯をカテナリー支持している方法を
とる(特公昭52−26723号公報)。
In order to prevent this pickup flaw, a method is adopted in which the hearth roll is made of asbestos, the number of rolls is minimized, and the stainless steel strip is catenary supported (Japanese Patent Publication No. 52-26723).

また、酸洗処理は脱スケール及び不動態化処理が施され
、従来は、中性塩電解、6肖酸電解、61’l酸及び硝
弗酸などを組み合わせて行われていた。
In addition, pickling treatment includes descaling and passivation treatment, and conventionally, it has been carried out using a combination of neutral salt electrolysis, 6-acid electrolysis, 61'l acid, nitric-fluoric acid, and the like.

〈発明が解決しようとするsun> しかしながら、上に述べた従来の連続焼鈍・酸洗部(i
iifにおいては、処理ラインが非常に長大なものとな
り、しかもその反面生産能力はさほど高くないというと
ころに問題を残していた。
<Sun problem to be solved by the invention> However, the conventional continuous annealing/pickling section (i.e.
In IIF, the processing line is very long, and on the other hand, the problem remains that the production capacity is not very high.

例えば、15T/I(の生産能力を出すためには、約4
5mのカテナリー型直火炉と約50mの酸洗槽、従って
、少なくとも約100 mに及ぶ長大な設備を必要とし
ていた。
For example, in order to produce a production capacity of 15T/I, approximately 4
This required a 5m long catenary-type direct-fired furnace and an approximately 50m pickling tank, which meant a long facility spanning at least approximately 100m.

また、炉内のアスベストロールは、ピックアップ疵の発
生を回避するために、1〜2回/月程度の交換を必要と
していた。
In addition, the asbestos roll in the furnace needed to be replaced about once or twice a month in order to avoid the occurrence of pick-up defects.

さらに、酸洗部においては、長大な酸洗槽と共に、液種
の異なる各酸洗槽ごとに給酸、循環装置などの付帯設備
を必要としていた。
Furthermore, the pickling section requires not only a long pickling tank but also ancillary equipment such as acid supply and circulation equipment for each pickling tank with a different type of liquid.

また、環境衛生上、排気処理設備、廃酸処理設備なども
必要とし、多岐に渡る設備のメンテナンスが極めて厄介
であった。
In addition, for environmental hygiene reasons, exhaust treatment equipment, waste acid treatment equipment, etc. are also required, making maintenance of the various equipment extremely troublesome.

本発明は、上記の諸問題を有利に解決するもので、生産
性に冨むステンレス鋼帯の連続焼鈍・酸洗方法を、コン
パクトでしかもメンテナンスが容易な設備と共に提案す
ることを目的とする。
The present invention advantageously solves the above-mentioned problems, and aims to propose a highly productive continuous annealing and pickling method for stainless steel strips, together with equipment that is compact and easy to maintain.

く課題を解決するための手段〉 第1の発明は、鋼41Fを、加熱帯から冷却帯まで順次
に搬送する間に所定の熱処理を施す連続焼鈍設備及び酸
洗設備によってステンレス鋼帯に焼鈍処理と酸洗処理と
を連続して施すに当たり、還元性雰囲気下に間接加熱に
よる焼鈍を施すと共に、引き続く酸洗を、少なくとも弗
化物を添加した硝酸水溶液、すなわち硝弗酸を電解液と
して使用する電解酸洗によって行うことを特徴とするス
テンレス鋼−!1Fの連続焼鈍・酸洗方法である。
Means for Solving the Problem> The first invention provides annealing treatment to a stainless steel strip using continuous annealing equipment and pickling equipment that perform predetermined heat treatment while sequentially conveying steel 41F from a heating zone to a cooling zone. In sequentially performing the pickling treatment, annealing is performed by indirect heating in a reducing atmosphere, and the subsequent pickling is performed by electrolysis using an aqueous nitric acid solution containing at least fluoride, that is, nitric-fluoric acid as the electrolyte. Stainless steel characterized by acid washing! This is a 1F continuous annealing/pickling method.

また、第2の発明は、加熱帯、冷却4tFを有する連続
焼鈍炉と酸洗設備とを併せ011えたステンレス鋼IF
の連続焼鈍・酸洗設備において、上記焼鈍炉の各帯域が
主として竪型炉からなり、かつ加熱帯が還元性雰囲気下
に間接加熱を施すように構成されており、上記酸洗設備
が少なくとも弗化物を添加した硝酸水溶液、すなわち硝
弗酸を電解液として使用する電解酸洗槽を有することを
特徴とするステンレス鋼IFの連続焼鈍・酸洗設備であ
る。
Further, the second invention is a stainless steel IF equipped with a heating zone, a continuous annealing furnace having a cooling capacity of 4 tF, and pickling equipment.
In the continuous annealing/pickling equipment, each zone of the annealing furnace is mainly composed of a vertical furnace, and the heating zone is configured to perform indirect heating in a reducing atmosphere, and the pickling equipment is configured to provide at least a fluorophore. This continuous annealing/pickling equipment for stainless steel IF is characterized by having an electrolytic pickling tank that uses a nitric acid aqueous solution containing a compound, that is, nitrofluoric acid, as an electrolyte.

〈作 用〉 本発明では、焼鈍炉の各帯域を主として竪型炉として構
成しているので、炉の上下には多数のハースロールが配
置されて、ステンレス鋼帯はこれらのハースロールに順
次巻き付けられて熱処理を施されるが、炉内は還元性雰
囲気に保持され、ラジアントチューブなどによる間接加
熱を行うので、炉内で酸化スケールが発生ずることは殆
どなく、従って、このように多数のハースロールを使用
しても酸化スケールのロールへの付着成長に起因したピ
ックアップ疵の発生の恐れは殆どなく、また、その後の
酸洗処理は、rli’l弗酸電解処理だけで充分である
<Function> In the present invention, each zone of the annealing furnace is configured mainly as a vertical furnace, so a large number of hearth rolls are arranged above and below the furnace, and the stainless steel strip is wound around these hearth rolls in sequence. However, since the inside of the furnace is maintained in a reducing atmosphere and indirect heating is performed using radiant tubes, there is almost no oxidation scale generated inside the furnace. Even if a roll is used, there is almost no risk of pick-up defects caused by the adhesion and growth of oxide scale on the roll, and the subsequent pickling treatment is only rli'l hydrofluoric acid electrolysis treatment.

〈実施例〉 第1図に、本発明に従うステンレス鋼帯の連続焼鈍・酸
洗設備の好適例を模式的に示す、この例は、焼鈍炉の各
1tF J)iとも竪型炉で構成した場合である0図中
番号1は予熱帯、2は加熱帯、3は均熱帯、4は冷却帯
、5は最終冷却装置であり、6は硫酸槽、7は硝弗酸電
解酸洗槽である。なお、8はスプレーやブラシ、スクラ
バーなどからなる清浄装置、9はドライヤーである。
<Example> Fig. 1 schematically shows a preferred example of continuous annealing and pickling equipment for stainless steel strip according to the present invention. In the figure, number 1 is the preheating zone, 2 is the heating zone, 3 is the soaking zone, 4 is the cooling zone, 5 is the final cooling device, 6 is the sulfuric acid tank, and 7 is the nitrofluoric acid electrolytic pickling tank. be. In addition, 8 is a cleaning device consisting of a spray, a brush, a scrubber, etc., and 9 is a dryer.

さて、上記の好適例では、焼鈍炉の各帯域をいずれも竪
型炉として構成しているので、炉の上下には多数のハー
スロールが配置されて、ステンレス鋼帯Sはこれらのハ
ースロールに順次巻き付けられて熱処理を施されること
になるが、炉内は11゜とNtなとの還元性雰囲気に保
持され、ラジアントチューブなどによる間接加熱を行う
ので、炉内で酸化スケールが発生することは殆どなく、
従ってこのように多数のハースロールを使用しても酸化
スケールのロールへの付着成長に起因したビックアンプ
疵の発生のおそれは殆どない。なお、雰囲気ガスとして
はh:3〜15%、Nt:残が適当である。
Now, in the above preferred example, each zone of the annealing furnace is configured as a vertical furnace, so a large number of hearth rolls are arranged above and below the furnace, and the stainless steel strip S is attached to these hearth rolls. They are wound one after the other and undergo heat treatment, but the inside of the furnace is maintained in a reducing atmosphere of 11° and Nt, and indirect heating is performed using a radiant tube, so there is no risk of oxidized scale forming inside the furnace. There are almost no
Therefore, even when such a large number of hearth rolls are used, there is almost no risk of occurrence of big amp defects due to the growth of oxide scale on the rolls. Note that as the atmospheric gas, h: 3 to 15%, Nt: balance is appropriate.

また、炉内は主として竪型炉であるため、ステンレス鋼
惜の炉内通過長さを大きくとることができ、従来の直火
式加熱から間接式加熱への変更というマイナス要因をは
るかに上回って、通板速度すなわち生産性を著しく向上
できるのみならず、炉長を大幅に短縮できる。また、従
来のように、アスベストロールのような高価なロールを
あえて使用する必要はない。
In addition, since the furnace is mainly a vertical furnace, the passage length of stainless steel through the furnace can be increased, which far outweighs the negative factor of changing from conventional direct heating to indirect heating. , it is possible not only to significantly improve the sheet passing speed, that is, productivity, but also to significantly shorten the furnace length. Further, there is no need to use expensive rolls such as asbestos rolls as in the past.

なお、第1図に示す好適例において、特に前記の問題が
発生しやすい加熱相中の高温部については、1バス炉を
横型とし、従来通りアスベスト製ハースロールによるカ
テナリー支持タイプを採用しても勿論よいが、鋼11F
を気体浮揚装置により非接触状態でのカテナリークイブ
を採用してもよい。
In addition, in the preferred example shown in Fig. 1, for the high-temperature part during the heating phase where the above-mentioned problem is particularly likely to occur, it is possible to use a horizontal one-bath furnace and adopt a catenary support type using asbestos hearth rolls as in the past. Of course it's good, but steel 11F
A non-contact catenary squib may be employed using a gas flotation device.

後前のタイプが本発明においてはより有効である。The back-front type is more effective in the present invention.

次に第2図に、第1図の焼鈍設備により焼鈍処理を施し
たステンレス鋼4jFを、Gli弗酸電解により酸洗処
理した場合の所要時間と電流密度との関係について調べ
た結果の一例を実線で示す。5US430テハ、?il
’(酸濃度20%、弗酸濃度5%、液温50°Cの硝弗
酸液を用い、一方5US304では、硼酸濃度20%、
弗酸濃度15%、液温60°Cの硝弗酸液を用いた。第
2図において、各[lII線の上方が酸洗良好域であり
、一方下方は酸洗不足域である。
Next, Figure 2 shows an example of the results of investigating the relationship between the required time and current density when stainless steel 4JF annealed using the annealing equipment shown in Figure 1 is pickled using Gli-hydrofluoric acid electrolysis. Indicated by solid line. 5US430 Teha? il
(Using a nitric-fluoric acid solution with an acid concentration of 20%, a hydrofluoric acid concentration of 5%, and a liquid temperature of 50°C; on the other hand, in 5US304, a boric acid concentration of 20%,
A nitric-fluoric acid solution with a hydrofluoric acid concentration of 15% and a liquid temperature of 60°C was used. In FIG. 2, the area above each [lII line is a good pickling area, while the area below is an insufficient pickling area.

第2図から明らかなように、電流密度が比較的高い場合
には2〜3秒で、また電流密度が低い場合でも10〜2
0秒で酸洗処理可能である。
As is clear from Figure 2, it takes 2 to 3 seconds when the current density is relatively high, and 10 to 2 seconds even when the current density is low.
Pickling treatment is possible in 0 seconds.

また、−点鎖線は濃度20%、温度70°Cの硫酸水溶
液に10秒浸漬させた後に、上述の硝弗酸液で電解酸洗
を行った場合の電流密度と酸洗時間との関係を示したも
のであり、その効果がはっきり表れることがわかる。す
なわち、61’1弗酸液を用いた電M酸洗の1)1■に
硫酸等による浸漬を行うことにより、電解酸洗時間を短
縮することができ、電極長を短くすることができる。
In addition, the - dotted line shows the relationship between current density and pickling time when electrolytic pickling is performed with the above-mentioned nitric-fluoric acid solution after immersion in a sulfuric acid aqueous solution with a concentration of 20% and a temperature of 70°C for 10 seconds. It can be seen that the effect is clearly visible. That is, by performing immersion in sulfuric acid or the like in step 1)1 of electrolytic pickling using a 61'1 hydrofluoric acid solution, the electrolytic pickling time can be shortened, and the electrode length can be shortened.

次に、第3図に、lil’l酸濃度20%、弗酸濃度5
%の硝弗酸の場合におい゛ζ良好な酸洗を達威し得る電
流密度と液温との関係につい°ririべた結果を示す
。なお、電解時間はいずれも2秒間とした。第3図より
、電流密度を低めにしたい場合には、液温を上昇させる
ことが酸洗性向上に有効であることがわかる。
Next, in Figure 3, lil'l acid concentration is 20%, hydrofluoric acid concentration is 5%,
% nitric hydrofluoric acid, the relationship between current density and liquid temperature that can achieve good pickling is shown below. In addition, the electrolysis time was 2 seconds in all cases. From FIG. 3, it can be seen that when it is desired to lower the current density, increasing the liquid temperature is effective in improving the pickling performance.

勿論、さらに硝弗酸電解酸洗における酸洗時の電流密度
を下げたい場合には、第2図に一点鎖線で示したように
、別の酸洗と組み合わせることが有効である。
Of course, if it is desired to further lower the current density during pickling in nitrofluoric acid electrolytic pickling, it is effective to combine it with another pickling, as shown by the dashed line in FIG.

なお、上述したように本発明では、連続焼鈍を還元性雰
囲気中で行うので、その後の酸洗処理は硝弗酸電解処理
だけでも充分である。
Note that, as described above, in the present invention, continuous annealing is performed in a reducing atmosphere, so that the subsequent pickling treatment may be performed simply by nitric-fluoric acid electrolytic treatment.

さらに、以上述べたことから明らかなように、本発明に
よる焼鈍炉は一般冷延鋼(IP用としてもそのまま使用
することができるので、ステンレス鋼帯と一般鋼・II
Fの兼用ラインとして大きな威力を発揮する。
Furthermore, as is clear from the above, the annealing furnace according to the present invention can be used as it is for general cold rolled steel (IP),
Demonstrates great power as a dual-purpose F line.

〈発明の効果〉 この発明の効果は、次のとおりに要約される。<Effect of the invention> The effects of this invention can be summarized as follows.

(1)処理能力が格段に向上すると共に、設備長さを大
幅に短縮できる。
(1) Processing capacity is significantly improved and equipment length can be significantly shortened.

(2)焼鈍炉の炉内雰囲気を還元性雰囲気にすると共に
、特に加熱g中の高温jtF域を非接触状態とすること
により、ピックアップ疵の発生を皆無にすることができ
る。
(2) By making the atmosphere inside the annealing furnace a reducing atmosphere and by making the high temperature jtF region in particular during heating g non-contact, it is possible to completely eliminate the occurrence of pick-up flaws.

(3)アスベストロールを使用する必要がないので、ロ
ール交換作業が不要となり、コスト削減となる。
(3) Since there is no need to use asbestos rolls, there is no need to replace rolls, resulting in cost reduction.

(4)酸化スケールがほとんどなくなるので、スケール
ロスによる歩留りの低下を防止できる。
(4) Since almost no oxide scale is present, a decrease in yield due to scale loss can be prevented.

(5)酸洗槽が少なくて済むので、薬液管理が容易であ
り、また、給酸、廃酸、循環設備などの付帯設備を大幅
に削減できる。
(5) Since fewer pickling tanks are required, chemical management is easy, and additional equipment such as acid supply, waste acid, and circulation equipment can be significantly reduced.

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

第1図は本発明によるステンレス鋼帯の連続焼鈍・酸洗
設備の模式図、第2図は本発明による聞弗酸電解処理に
おける処理時間と1を流密度との関係を示したグラフ、
第3図は鞘部電解酸洗における電流密度と液温との関係
を示したグラフである。 1・・・予熱帯、 3・・・均熱杏、 5・・・層材冷却装置、 7・・・硝弗酸電解酸洗槽、 9・・・乾燥装置、 2・・・加熱帯、 4・・・冷却帯、 6・・・硫酸浸漬槽、 8・・・清浄装置、 S・・・ステンレスm帯。 第 図 液 温(°C)
FIG. 1 is a schematic diagram of continuous annealing and pickling equipment for stainless steel strip according to the present invention, and FIG. 2 is a graph showing the relationship between treatment time and flow density in hydrofluoric acid electrolytic treatment according to the present invention.
FIG. 3 is a graph showing the relationship between current density and liquid temperature in sheath electrolytic pickling. DESCRIPTION OF SYMBOLS 1... Pre-heating zone, 3... Soaking apricot, 5... Layer material cooling device, 7... Nitrofluoric acid electrolytic pickling tank, 9... Drying device, 2... Heating zone, 4... Cooling zone, 6... Sulfuric acid immersion tank, 8... Cleaning device, S... Stainless steel m band. Diagram: Liquid temperature (°C)

Claims (2)

【特許請求の範囲】[Claims] (1)鋼帯を、加熱帯から冷却帯まで順次に搬送する間
に所定の熱処理を施す連続焼鈍設備及び酸洗設備によっ
てステンレス鋼帯に焼鈍処理と酸洗処理とを連続して施
すに当たり、還元性雰囲気下に間接加熱による焼鈍を施
すと共に、引き続く酸洗を、少なくとも弗化物を添加し
た硝酸水溶液を電解液として使用する電解酸洗によって
行うことを特徴とするステンレス鋼帯の連続焼鈍・酸洗
方法。
(1) When sequentially subjecting a stainless steel strip to annealing treatment and pickling treatment using continuous annealing equipment and pickling equipment that perform predetermined heat treatment while sequentially transporting the steel strip from the heating zone to the cooling zone, Continuous annealing/acidification of a stainless steel strip, characterized in that annealing is performed by indirect heating in a reducing atmosphere, and subsequent pickling is performed by electrolytic pickling using an aqueous nitric acid solution containing at least fluoride as an electrolyte. Washing method.
(2)加熱帯、冷却帯を有する連続焼鈍炉と酸洗設備と
を併せ備えたステンレス鋼帯の連続焼鈍・酸洗設備にお
いて、上記焼鈍炉の各帯域が主として竪型炉からなり、
かつ加熱帯が還元性雰囲気下に間接加熱を施すように構
成されており、上記酸洗設備が少なくとも弗化物を添加
した硝酸水溶液を電解液として使用する電解酸洗槽を有
することを特徴とするステンレス鋼帯の連続焼鈍・酸洗
設備。
(2) In a continuous annealing/pickling facility for stainless steel strips, which is equipped with a continuous annealing furnace having a heating zone and a cooling zone, and a pickling facility, each zone of the annealing furnace mainly consists of a vertical furnace;
and the heating zone is configured to perform indirect heating in a reducing atmosphere, and the pickling equipment has an electrolytic pickling tank that uses at least a fluoride-added nitric acid aqueous solution as an electrolyte. Continuous annealing and pickling equipment for stainless steel strips.
JP21506989A 1989-08-23 1989-08-23 Method and apparatus for continuously annealing and pickling stainless steel strip Pending JPH0379795A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21506989A JPH0379795A (en) 1989-08-23 1989-08-23 Method and apparatus for continuously annealing and pickling stainless steel strip

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21506989A JPH0379795A (en) 1989-08-23 1989-08-23 Method and apparatus for continuously annealing and pickling stainless steel strip

Publications (1)

Publication Number Publication Date
JPH0379795A true JPH0379795A (en) 1991-04-04

Family

ID=16666242

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21506989A Pending JPH0379795A (en) 1989-08-23 1989-08-23 Method and apparatus for continuously annealing and pickling stainless steel strip

Country Status (1)

Country Link
JP (1) JPH0379795A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04311531A (en) * 1991-04-09 1992-11-04 Mitsubishi Heavy Ind Ltd Annealing and pickling equipment for stainless steel sheet
WO2008058986A1 (en) * 2006-11-14 2008-05-22 Danieli & C. Officine Meccaniche S.P.A. Annealing and pickling process

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62124232A (en) * 1985-08-08 1987-06-05 Kawasaki Steel Corp Method and equipment for continuously annealing and pickling stainless steel strip
JPS62294200A (en) * 1986-06-12 1987-12-21 Kawasaki Steel Corp Method for electrolytically pickling cold rolled and annealed stainless steel strip
JPS63297599A (en) * 1987-05-29 1988-12-05 Kawasaki Steel Corp Method for removing scale of stainless steel

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62124232A (en) * 1985-08-08 1987-06-05 Kawasaki Steel Corp Method and equipment for continuously annealing and pickling stainless steel strip
JPS62294200A (en) * 1986-06-12 1987-12-21 Kawasaki Steel Corp Method for electrolytically pickling cold rolled and annealed stainless steel strip
JPS63297599A (en) * 1987-05-29 1988-12-05 Kawasaki Steel Corp Method for removing scale of stainless steel

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04311531A (en) * 1991-04-09 1992-11-04 Mitsubishi Heavy Ind Ltd Annealing and pickling equipment for stainless steel sheet
WO2008058986A1 (en) * 2006-11-14 2008-05-22 Danieli & C. Officine Meccaniche S.P.A. Annealing and pickling process
CN101558173A (en) * 2006-11-14 2009-10-14 丹尼利机械设备股份公司 Annealing and pickling process
US8192566B2 (en) 2006-11-14 2012-06-05 Danieli & C. Officine Meccaniche S.P.A. Annealing and pickling process

Similar Documents

Publication Publication Date Title
CN100409957C (en) Bandes en acier inoxydable austenitique d&#39;aspect de surface mat
US4713154A (en) Continuous annealing and pickling method and apparatus for steel strips
WO2023000521A1 (en) Cold-rolled, stainless steel annealing and pickling process and pickling device
PL179348B1 (en) Method of annealing stainless steels and removing scale from their surfaces
JPS5591945A (en) Method and equipment for cooling of steel strip in continuous annealing line
US4143184A (en) Production of galvanized steel strip
JPS5996300A (en) Control of oxidated scale formation and method of descaling metal products
JPS62124232A (en) Method and equipment for continuously annealing and pickling stainless steel strip
JPH0379795A (en) Method and apparatus for continuously annealing and pickling stainless steel strip
JPH0379796A (en) Method and equipment for continuously annealing and pickling stainless steel strip
JPH0379797A (en) Method and equipment for continuously annealing and pickling stainless steel strip
US5783000A (en) Method for heat treatment of steel, and products of steel
CA1259050A (en) Method and apparatus for the continuous annealing of steel strips
JPH01162786A (en) Method for pickling high strength austenitic stainless steel
JPH11279781A (en) Production of austenitic stailness steel plate not having pattern on surface
JPH06108164A (en) Method for cooling annealed coil
JP2640565B2 (en) Continuous production equipment for stainless steel sheets
JP2986670B2 (en) Apparatus and method for producing Cr-containing corrosion-resistant steel strip
JPS6325080B2 (en)
JPS5591929A (en) Method and facility for continuous annealing of cold rolled steel strip
JPH11158699A (en) Method for descaling stainless steel strip and its continuous production device
JPH0525666A (en) Manufacture of austenitic stainless steel strip
JPS5920752B2 (en) Pickling method for austenitic stainless steel sheet
JPH0313529A (en) Method for annealing stainless steel
JPS5842251B2 (en) Continuous processing equipment for non-oriented electrical steel strip