JPH0241599B2 - - Google Patents
Info
- Publication number
- JPH0241599B2 JPH0241599B2 JP13699586A JP13699586A JPH0241599B2 JP H0241599 B2 JPH0241599 B2 JP H0241599B2 JP 13699586 A JP13699586 A JP 13699586A JP 13699586 A JP13699586 A JP 13699586A JP H0241599 B2 JPH0241599 B2 JP H0241599B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolytic
- nitric acid
- stainless steel
- descaling
- rolled
- 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
Links
- 238000000034 method Methods 0.000 claims description 27
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 25
- 229910017604 nitric acid Inorganic materials 0.000 claims description 25
- 238000005554 pickling Methods 0.000 claims description 23
- 239000010935 stainless steel Substances 0.000 claims description 23
- 229910001220 stainless steel Inorganic materials 0.000 claims description 23
- 150000002222 fluorine compounds Chemical class 0.000 claims description 13
- 229910000831 Steel Inorganic materials 0.000 claims description 10
- 239000010959 steel Substances 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 8
- 238000011282 treatment Methods 0.000 claims description 8
- 239000008151 electrolyte solution Substances 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 4
- 229910017855 NH 4 F Inorganic materials 0.000 claims description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 238000000137 annealing Methods 0.000 description 19
- 239000003792 electrolyte Substances 0.000 description 8
- 238000005868 electrolysis reaction Methods 0.000 description 7
- 238000007654 immersion Methods 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 6
- 230000001590 oxidative effect Effects 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000000523 sample Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000001447 alkali salts Chemical class 0.000 description 3
- 229910052731 fluorine Inorganic materials 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000002161 passivation Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000010960 cold rolled steel Substances 0.000 description 2
- 238000005097 cold rolling Methods 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 229960002050 hydrofluoric acid Drugs 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000001294 propane Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002436 steel type Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000011866 long-term treatment Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 238000005502 peroxidation Methods 0.000 description 1
- 235000021110 pickles Nutrition 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 238000004383 yellowing Methods 0.000 description 1
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
〔産業上の利用分野〕
本発明はステンレス冷延、焼鈍鋼帯の電解酸洗
方法に係り、特にステンレス冷延鋼帯の焼鈍後の
表面スケールを短時間で除去する電解酸洗方法に
関し、ステンレス冷延鋼帯の製造分野で利用され
る。
〔従来の技術〕
冷間圧延後のステンレス鋼帯は、主として圧延
歪を除去し、かつ諸特性を改善する目的で焼鈍さ
れる。従来の焼鈍方法としては、水素雰囲気もし
くは(水素+窒素)雰囲気などの還元性雰囲気中
でのいわゆる光輝焼鈍と、プロパンガスやコーク
ス炉ガス等の酸化性燃焼ガス雰囲気中で連続的に
焼鈍する方法とがあるが、近年、生産性を高める
ために普通鋼の連続焼鈍ライン(以下CALと称
する)が用いられるようになつた。
これらの焼鈍方法のうち、燃焼ガスによる場合
と、CALによる場合には、酸化性雰囲気中の焼
鈍であるので表面に酸化皮膜、すなわちスケール
が形成される。これらのスケールは、特にCAL
による場合のスケールは、一般にテンパーカラー
と称され非常に薄いものであるが、それでも酸化
皮膜のついたままでは耐食性が劣り、またプレス
作業等で型の摩耗が著しく問題となるので除去す
る必要がある。そのために通常酸洗処理を行う
か、もしくはベルトグラインダーによる研削を行
なつている。スケールは厚さが薄いが非常に緻密
かつ強固なものであつて除去し難く、そのため酸
洗工程も複雑である。
従来、連続焼鈍後のステンレス冷延鋼の連続脱
スケール方法としては、NaOH、NaCO3を主成
分とする溶融アルカリ塩に浸漬するソルト処理、
あるいはNa2SO4、Na2NO3等の中性塩溶液中に
おける電解処理などの前処理を行なつてCr+3を
Cr+6に変化させた後、硫酸、硝弗酸(硝酸+弗化
水素酸)、硝酸等の水溶液に浸漬するか、または
硫酸水溶液中もしくは硝酸水溶液中での電解処理
を付加する方法が採用されていた。特開昭59−
59900、特公昭38−12162などに開示されたこれら
の浸漬もしくは電解方法は、鋼種や焼鈍条件の差
によつて生ずる脱スケールの難易度によつて使い
分けるのが一般的である。
しかしこれらの場合にも完全に脱スケールする
にはなおも長時間を要し、ステンレス冷延鋼帯の
生産能率を阻害する原因となつている。脱スケー
ル性を保持しつつ、ライン速度を上げるには、上
記の如く溶融アルカリ塩および各種の酸への浸漬
時間、電解時間などを確保するために、各種浸漬
槽、電解槽を長大化する必要があり、それには多
額の設備投資とそれを設置するための広大な屋内
スペースが必要となり、現実には、低い通板速度
で対処されていた。また、多種類の塩類や酸を用
いるため、その濃度管理等も負荷の大きいもので
ある。かくの如くステンレス冷延、焼鈍鋼帯の脱
スケール従来いずれの方法によつても問題点があ
つた。
〔発明が解決しようとする問題点〕
本発明の目的は、ステンレス冷延、焼鈍鋼帯の
脱スケールにおける上記従来技術の問題点、なわ
ち低い生産性、繁雑な工程管理を解消して、一液
による高能率の脱スケール方法を提供するにあ
る。
〔問題点を解決するための手段および作用〕
本発明の要旨とするところは次の如くである。
すなわち、硝酸を電解液として電解処理するステ
ンレス冷延、焼鈍鋼帯の電解酸洗方法において、
前記電解液として硝酸に弗素化合物を添加た水溶
液を用いることを特徴とするステンレス冷延、焼
鈍鋼帯の電解酸洗方法である。
一般にステンレス鋼は、その材料機能としての
高耐食性を付与するために、通常酸洗の最終工程
で硝酸による不働態化処理を施している。この不
働態化処理は硝酸への浸漬もしくは硝酸による電
解によつて達成されるが、この処理はステンレス
鋼の機能を確保する上において不可欠の工程であ
る。
ステンレス鋼を不働態化するためには酸化性酸
への浸漬が有効であり、そのために工業的な規模
での実用性から硝酸が用いられる。電解質として
は、硝酸中での解離定数の大きいものほど有効で
あるが、硝酸塩では脱スケール効果が小さくま
た、塩化物では均一な脱スケールが達成できな
い。
本発明者らは一液による高能率脱スケールを行
うために、硝酸による電解条件に関して広範な実
験を行なつたが、特に硝酸による電解効率を高め
るための電解液組成について研究した結果、硝酸
に弗素化合物の添加が有効であるとの知見を得た
ので、この知見に基いて更に研究を重ね本発明を
完成するに至つたものである。
ステンレス冷延、焼鈍鋼帯の硝酸を電解液とす
る電解酸洗に際しては、ステンレス冷延鋼板の焼
鈍条件により電流密度、電解時間などが多少異な
るものの、水素もしくは(水素+窒素)雰囲気中
での低い酸化性雰囲気中の焼鈍板および酸化性雰
囲気中の焼鈍板は、本発明による弗素化合物を添
加した硝酸水溶液を電解液とする場合、比較的短
時間にしかも確実に脱スケールされることが判明
した。
添加する弗素化合物はどのようなものであつて
も脱スケール性に差はないが、工業的な利用の観
点からは、KF、NH4F、NH4HF2、
(NH4)3FeF6、HFのうちから選ばれることが好
ましい。
この場合弗素化合物の添加量は弗素当量で0.3
〜5%の範囲に限定する。その理由は弗素化合物
の添加量が微量添加であつても、電解電流密度の
増加、電解浴温度の上昇により脱スケール能率が
向上するが、0.3%未満では電流密度が50A/d
m2以上、温度を60℃以上に上げても脱スケールが
困難であるばかりではなく、電流密度および温度
の上昇に基づく過酸化現象が起り、表面が黄変す
る欠陥が現れるので下限を0.3%とした。また添
加量が過度に多くなつて5%を越すと、酸洗浴の
温度を常温としても、反応熱より過酸洗となつて
ステンレス鋼の表面肌を荒すので上限を弗素当量
で5%と限定すべきである。
しかしてこの場合の硝酸濃度は5%未満では弗
素化合物添加の効果が小さく、20%を越えると脱
スケール反応と共にNOxの生が認められたので
上限を20%とし、5〜20%の範囲に限定した。
〔実施例〕
冷間圧延後の各種ステンレス鋼帯を、実工程の
連続焼鈍ラインCALもしくは焼鈍酸洗ライン
(以下APLと称する)で連続焼鈍したままの状態
のものを供試材とし、焼鈍雰囲気、温度等の焼鈍
条件を変化させ、各供試材表面上にスケールを発
生させた後、本発明の要件の電解液組成および本
発明外の要件にて電解酸洗し、スケールの除去状
況を比較する比較試験を行つた。供試材としては
JIS規格SUH409、SUS430およびSUS304の3鋼
種を使用し、APLでは酸洗ラインをバイパスさ
せた。各供試材の焼鈍条件および発生スケールの
状態は第1表に示すとおりである。
[Industrial Application Field] The present invention relates to an electrolytic pickling method for stainless steel cold rolled and annealed steel strips, and more particularly to an electrolytic pickling method for removing surface scale after annealing of stainless steel cold rolled steel strips in a short time. Used in the field of manufacturing cold rolled steel strips. [Prior Art] A stainless steel strip after cold rolling is annealed mainly for the purpose of removing rolling strain and improving various properties. Conventional annealing methods include so-called bright annealing in a reducing atmosphere such as a hydrogen atmosphere or (hydrogen + nitrogen) atmosphere, and continuous annealing in an oxidizing combustion gas atmosphere such as propane gas or coke oven gas. However, in recent years, continuous annealing lines (hereinafter referred to as CAL) for ordinary steel have come into use to increase productivity. Among these annealing methods, when using combustion gas and when using CAL, an oxide film, that is, scale, is formed on the surface because the annealing is performed in an oxidizing atmosphere. These scales are especially suitable for CAL
The scale caused by molding is generally called temper color and is very thin, but if the oxide film remains on it, it has poor corrosion resistance and mold wear during press work etc. becomes a serious problem, so it must be removed. be. For this purpose, pickling treatment or grinding with a belt grinder is usually performed. Although the scale is thin, it is very dense and strong and difficult to remove, making the pickling process complicated. Conventionally, continuous descaling methods for cold-rolled stainless steel after continuous annealing include salt treatment by immersion in molten alkali salts mainly composed of NaOH and NaCO3 ;
Alternatively, Cr +3 can be removed by pretreatment such as electrolytic treatment in a neutral salt solution such as Na 2 SO 4 or Na 2 NO 3 .
After changing to Cr +6 , it is immersed in an aqueous solution of sulfuric acid, nitric-fluoric acid (nitric acid + hydrofluoric acid), nitric acid, or electrolytically treated in an aqueous sulfuric acid solution or an aqueous nitric acid solution. It had been. Unexamined Japanese Patent Publication 1983-
59900, Japanese Patent Publication No. 38-12162, etc., these immersion or electrolytic methods are generally used depending on the difficulty of descaling caused by differences in steel type and annealing conditions. However, even in these cases, it still takes a long time to completely descale, which is a cause of inhibiting the production efficiency of cold-rolled stainless steel strips. In order to increase the line speed while maintaining descaling performance, it is necessary to increase the length of various immersion tanks and electrolytic tanks in order to ensure the immersion time in molten alkali salts and various acids, electrolysis time, etc. as described above. This requires a large amount of capital investment and a large indoor space to install it, which in reality has been dealt with by low threading speeds. In addition, since many types of salts and acids are used, controlling their concentrations is a heavy burden. As described above, both conventional methods of descaling cold-rolled and annealed stainless steel strips have had problems. [Problems to be Solved by the Invention] The purpose of the present invention is to solve the above-mentioned problems of the prior art in descaling stainless steel cold-rolled and annealed steel strips, that is, low productivity and complicated process control. The purpose of the present invention is to provide a highly efficient descaling method using a liquid. [Means and effects for solving the problems] The gist of the present invention is as follows.
That is, in an electrolytic pickling method for cold-rolled stainless steel and annealed steel strip, which is electrolytically treated using nitric acid as an electrolyte,
This is an electrolytic pickling method for cold-rolled and annealed stainless steel strip, characterized in that an aqueous solution containing a fluorine compound added to nitric acid is used as the electrolytic solution. Generally, stainless steel is subjected to passivation treatment with nitric acid in the final step of pickling, in order to impart high corrosion resistance as a material function. This passivation treatment is achieved by immersion in nitric acid or electrolysis with nitric acid, and this treatment is an essential step in ensuring the functionality of stainless steel. In order to passivate stainless steel, immersion in oxidizing acid is effective, and nitric acid is used for practicality on an industrial scale. As an electrolyte, the larger the dissociation constant in nitric acid, the more effective it is, but nitrates have a small descaling effect, and chlorides cannot achieve uniform descaling. In order to perform high-efficiency descaling with a single solution, the present inventors conducted extensive experiments on electrolytic conditions using nitric acid. Since we found that the addition of a fluorine compound is effective, we conducted further research based on this knowledge and completed the present invention. When electrolytically pickling cold-rolled stainless steel and annealed steel strips using nitric acid as the electrolyte, the current density and electrolysis time may vary slightly depending on the annealing conditions of the cold-rolled stainless steel sheets, but it is possible to pickle them in a hydrogen or (hydrogen + nitrogen) atmosphere. It has been found that plates annealed in a low oxidizing atmosphere and plates annealed in an oxidizing atmosphere can be descaled in a relatively short time and reliably when an aqueous nitric acid solution containing a fluorine compound according to the present invention is used as an electrolyte. did. There is no difference in descaling performance no matter what kind of fluorine compound is added, but from the viewpoint of industrial use, KF, NH 4 F, NH 4 HF 2 ,
It is preferably selected from (NH 4 ) 3 FeF 6 and HF. In this case, the amount of fluorine compound added is 0.3 in terms of fluorine equivalent.
-5% range. The reason for this is that even if the amount of fluorine compound added is very small, the descaling efficiency is improved by increasing the electrolytic current density and the temperature of the electrolytic bath, but when the amount is less than 0.3%, the current density is 50 A/d
m 2 or more, even if the temperature is raised to 60°C or more, descaling is not only difficult, but also a peroxidation phenomenon occurs due to the increase in current density and temperature, and defects such as yellowing of the surface appear, so the lower limit is set at 0.3%. And so. Furthermore, if the amount added exceeds 5%, even if the temperature of the pickling bath is room temperature, the reaction heat will cause overpickling and roughen the surface of the stainless steel, so the upper limit is limited to 5% in terms of fluorine equivalent. Should. However, if the nitric acid concentration in this case is less than 5%, the effect of adding a fluorine compound is small, and if it exceeds 20%, descaling reaction and NOx production were observed, so the upper limit was set at 20%, and the range of 5 to 20% was set. Limited. [Example] Various stainless steel strips after cold rolling were continuously annealed in the actual continuous annealing line CAL or annealing pickling line (hereinafter referred to as APL) as test materials, and the annealing atmosphere was After changing the annealing conditions such as temperature and generating scale on the surface of each sample material, electrolytic pickling was performed using the electrolyte composition according to the requirements of the present invention and requirements outside the present invention, and the scale removal status was evaluated. A comparative test was conducted to compare. As a sample material
Three types of steel, JIS standard SUH409, SUS430 and SUS304, were used, and the pickling line was bypassed in APL. The annealing conditions and the state of scale generated for each sample material are shown in Table 1.
【表】
第1表より明らかなとおり、CALで連続焼鈍
したSUH409、SUS430のスケールは前者の場合、
薄黄色、後者の場合、紫色、のいわゆるテンパー
カラーである。一方、APLで連続焼鈍した
SUH409、SUS430及びSUS304のスケールは、前
2者は光沢のある濃い青色、後者は光沢のない黄
褐色を呈しており、これらのスケール厚さは前記
したCALでの焼鈍による鋼板のスケールに比べ
ればかなり厚い。
第1表にて示したスケール状態の異なる各供試
材を本発明要件および本発明外条件にて電解酸洗
した時の電解液組成、温度、電流密度および実験
結果はそれぞれ第2、3、4、5、6表に示すと
おりである。
第2〜6表における本発明例および比較例はい
ずれもモデル酸洗槽によるものである。また、こ
れらの表に示す電解液組成はいずれも重量%であ
り、F当量%を併記した。更に実験結果は電解時
間を記載時間にそれぞれ変化せしめたものについ
ての脱スケール判定を示すものである。しかして
その判定は完全に脱スケールした代表サンプルと
対比して決定した目視判定の結果であり、各表中
の記号は第7表に示す如き意味を有するものであ
る。[Table] As is clear from Table 1, the scale of SUH409 and SUS430 continuously annealed by CAL is
The color is pale yellow, or in the latter case, purple, a so-called temper color. On the other hand, continuous annealing with APL
The scales of SUH409, SUS430, and SUS304 are shiny deep blue in the former, and dull yellowish brown in the latter.The thickness of these scales is compared to the scale of the steel plate annealed by CAL mentioned above. Quite thick. The electrolytic solution composition, temperature, current density, and experimental results when each test material with different scale states shown in Table 1 were electrolytically pickled under the requirements of the present invention and conditions outside the present invention are shown in the second, third, and third tables, respectively. As shown in Tables 4, 5, and 6. The invention examples and comparative examples in Tables 2 to 6 are all based on model pickling tanks. Furthermore, the electrolytic solution compositions shown in these tables are all weight %, and F equivalent % is also written. Furthermore, the experimental results show the descaling determination for different electrolysis times as described. However, the judgment is the result of visual judgment determined by comparison with a completely descaled representative sample, and the symbols in each table have the meanings shown in Table 7.
【表】
第2〜6表に示す本発明例1〜5、および比較
例1〜5の実験結果より明らかなとおり、5〜20
%の硝酸水溶液にF当量で0.3〜5%弗素化合物
を添加した電解液による本発明例は、硝酸単味の
水溶液もしくは硝酸に塩化物もしくは硝酸塩を添
加した電解液による比較例に比し、脱スケール性
能が明らかにすぐれていることを示している。
ここで留意すべきことは、第5表、第6表にて
示したプロパンガス燃焼による酸化性雰囲気中で
焼鈍したSUS430およびSUS304の脱スケール時
間は特開昭59−59900等の従来法に比して大幅に
短縮されていることである。しかも、これらの鋼
帯は特開昭59−59900によつて示された実験材と
同一ラインで焼鈍されたステンレス冷延、焼鈍鋼
帯であつて、十分に成長したスケールが形成され
ているものである。すなわち、特開昭59−59900
よる従来法は、例えばSUS430の場合、溶融アル
カリ塩浸漬の前処理を行つた後、硫酸水溶液に浸
漬し、更に硝酸水溶液で電解する方法であつて、
脱スケール時間は少くとも45秒要しているが、本
発明法による一液による電解では30秒以下で脱ス
ケールされている。SUS304の場合も、特開昭59
−59900による従来法では、4段階の酸洗工程を
必要とし、全工程で30秒程度要しているが、本発
明法によれば20秒で脱スケールが可能であつた。[Table] As is clear from the experimental results of Invention Examples 1 to 5 and Comparative Examples 1 to 5 shown in Tables 2 to 6, 5 to 20
The present invention example using an electrolytic solution in which 0.3 to 5% fluorine compound is added in F equivalent to a nitric acid aqueous solution has a higher desorption rate than the comparative example using an aqueous solution of nitric acid alone or an electrolytic solution in which chloride or nitrate is added to nitric acid. This shows that the scale performance is clearly superior. It should be noted here that the descaling time of SUS430 and SUS304 annealed in an oxidizing atmosphere by propane gas combustion shown in Tables 5 and 6 is comparable to that of conventional methods such as JP-A-59-59900. This means that it has been significantly shortened. Moreover, these steel strips are cold-rolled stainless steel strips annealed on the same line as the experimental material shown in JP-A-59-59900, and have sufficiently grown scales. It is. That is, JP-A-59-59900
For example, in the case of SUS430, the conventional method is to perform a pretreatment of immersion in a molten alkali salt, then immerse it in an aqueous sulfuric acid solution, and then electrolyze it in an aqueous nitric acid solution.
Although descaling time requires at least 45 seconds, descaling can be achieved in 30 seconds or less using one-liquid electrolysis according to the method of the present invention. In the case of SUS304, JP-A-59
The conventional method using -59900 required a four-stage pickling process, and the entire process took about 30 seconds, but the method of the present invention enabled descaling in 20 seconds.
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
ステンレス冷延鋼帯のCALもしくはAPLによ
る連続焼鈍もしくは焼鈍、酸洗工程における従来
の脱スケール方法は複数の酸洗工程による長時間
処理を余儀なくされて来たが、本発明による電解
酸洗方法は、従来の硝酸単味の水溶液を電解液と
する方法を廃して、電解液として硝酸に弗素化合
物を添加した水溶液を用いることにしたので、次
の如き大きな効果を挙げることができた。
(イ) 一液による脱スケールが可能となつたので、
工程を大幅に簡素化できた。
(ロ) 均一な完全脱スケールが可能となつた。
(ハ) 脱スケール時間を従来より短縮できるので、
比較的スケールの薄いCAL材については高速
通板が可能となり、生産性の向上が可能となつ
た。
(ニ) (イ)、(ロ)、(ハ)の結果脱スケールコストを大幅
に
低減できる。
本発明はステンレス冷延、焼鈍鋼帯の酸洗の最
終工程における硝酸による不働態化処理等に際
し、硝酸に弗素化合物を添加した水溶液を用いて
電解することを提案したもので、本発明法単独で
実施できることは勿論、従来の酸洗法と組合わせ
ても適用可能であることは自明のとおりである。
なお、電解による脱スケールの要件としては、
電解液温度、電流密度、電解時間等も当然関係す
るものではあるが、これらの要件は鋼種、焼鈍条
件の差異によつて生ずるスケール厚さに依存する
ものであるので、特に限定の必要がなく、本発明
による脱スケール方法はステンレスのすべての鋼
種に適用可能である。
Conventional descaling methods in the continuous annealing or annealing and pickling process of cold-rolled stainless steel strip using CAL or APL have required long-term treatment with multiple pickling processes, but the electrolytic pickling method according to the present invention By abolishing the conventional method of using a simple aqueous solution of nitric acid as an electrolyte and using an aqueous solution of nitric acid with a fluorine compound added as the electrolyte, we were able to achieve the following great effects. (b) Since descaling with one liquid became possible,
The process was greatly simplified. (b) Uniform and complete descaling became possible. (c) Descaling time can be reduced compared to conventional methods,
High-speed threading is now possible for CAL materials with relatively thin scales, making it possible to improve productivity. (d) As a result of (a), (b), and (c), descaling costs can be significantly reduced. The present invention proposes electrolyzing using an aqueous solution of nitric acid with a fluorine compound added to it during passivation treatment with nitric acid in the final pickling process of stainless steel cold-rolled and annealed steel strips. It is obvious that it can be applied not only in combination with conventional pickling methods, but also in combination with conventional pickling methods. The requirements for descaling by electrolysis are as follows:
Although electrolyte temperature, current density, electrolysis time, etc. are of course related, these requirements do not need to be particularly limited because they depend on the scale thickness caused by differences in steel type and annealing conditions. The descaling method according to the present invention is applicable to all types of stainless steel.
Claims (1)
冷延、焼鈍鋼帯の電解酸洗方法において、前記電
解液として硝酸に弗素化合物を添加した水溶液を
用いることを特徴とするステンレス冷延、焼鈍鋼
帯の電解酸洗方法。 2 前記弗素化合物はKF、NH4F、NH4HF2、
(NH4)3FeF6、HFのうちより選ばれたいずれか
である特許請求の範囲の第1項に記載のステンレ
ス冷延、焼鈍鋼帯の電解酸洗方法。 3 前記硝酸濃度は5〜20%であり、弗素化合物
濃度が弗素イオン当り0.3〜5%である特許請求
の範囲の第1項もしくは第2項に記載のステンレ
ス冷延、焼鈍鋼帯の電解酸洗方法。[Scope of Claims] 1. A method for electrolytic pickling of cold-rolled or annealed stainless steel strip in which nitric acid is used as an electrolytic solution for electrolytic treatment, characterized in that an aqueous solution of nitric acid and a fluorine compound added is used as the electrolytic solution. Electrolytic pickling method for rolled and annealed steel strip. 2 The fluorine compounds include KF, NH 4 F, NH 4 HF 2 ,
The method for electrolytic pickling of cold-rolled and annealed stainless steel strip according to claim 1, which is any one selected from (NH 4 ) 3 FeF 6 and HF. 3. Electrolytic acid for cold rolled and annealed stainless steel strip according to claim 1 or 2, wherein the nitric acid concentration is 5 to 20% and the fluorine compound concentration is 0.3 to 5% per fluorine ion. Washing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13699586A JPS62294200A (en) | 1986-06-12 | 1986-06-12 | Method for electrolytically pickling cold rolled and annealed stainless steel strip |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13699586A JPS62294200A (en) | 1986-06-12 | 1986-06-12 | Method for electrolytically pickling cold rolled and annealed stainless steel strip |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62294200A JPS62294200A (en) | 1987-12-21 |
| JPH0241599B2 true JPH0241599B2 (en) | 1990-09-18 |
Family
ID=15188326
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13699586A Granted JPS62294200A (en) | 1986-06-12 | 1986-06-12 | Method for electrolytically pickling cold rolled and annealed stainless steel strip |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62294200A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003082495A (en) | 2001-09-12 | 2003-03-19 | Chemical Yamamoto:Kk | Stainless steel with fluorine or fluorine and oxygen- containing film layer formed thereon, and production method therefor |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0379795A (en) * | 1989-08-23 | 1991-04-04 | Kawasaki Steel Corp | Method and apparatus for continuously annealing and pickling stainless steel strip |
| KR100368207B1 (en) * | 1995-12-11 | 2003-05-09 | 주식회사 포스코 | Electrolytic Dissolution of Austenitic Stainless Steel Annealed Steel Sheet |
| JP5309385B2 (en) * | 2007-04-27 | 2013-10-09 | 日本金属株式会社 | Stainless steel conductive member and manufacturing method thereof |
-
1986
- 1986-06-12 JP JP13699586A patent/JPS62294200A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003082495A (en) | 2001-09-12 | 2003-03-19 | Chemical Yamamoto:Kk | Stainless steel with fluorine or fluorine and oxygen- containing film layer formed thereon, and production method therefor |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62294200A (en) | 1987-12-21 |
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