JPS61264195A - Production of tin-free steel for retort can - Google Patents

Production of tin-free steel for retort can

Info

Publication number
JPS61264195A
JPS61264195A JP10467385A JP10467385A JPS61264195A JP S61264195 A JPS61264195 A JP S61264195A JP 10467385 A JP10467385 A JP 10467385A JP 10467385 A JP10467385 A JP 10467385A JP S61264195 A JPS61264195 A JP S61264195A
Authority
JP
Japan
Prior art keywords
treatment
reverse
electrode
chromium
steel sheet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP10467385A
Other languages
Japanese (ja)
Other versions
JPH0421759B2 (en
Inventor
Hisakatsu Kato
寿勝 加藤
Toshio Yokoyama
俊夫 横山
Fumio Kokado
古角 文雄
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 JP10467385A priority Critical patent/JPS61264195A/en
Publication of JPS61264195A publication Critical patent/JPS61264195A/en
Publication of JPH0421759B2 publication Critical patent/JPH0421759B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To produce a tin-free steel having excellent retort treatment resistance by subjecting a steel sheet to a cathodic treatment in an electrode for reverse electrolysis, Cr plating treatment, reverse electrolytic treatment and electrolytic Cr acid treatment. CONSTITUTION:The steel sheet as a cathode is subjected to the cathodic treatment at 7A/dm<2> current density in an aq. Cr acid soln. in the electrode for the reverse electrolytic treatment. The cold rolled steel sheet is successively immersed for 10sec in a 5% NaOH soln. at 70 deg.C and 8A/dm<2> current density and is then washed. Such steel sheet is subjected to the cathodic treatment for 1.2sec in a plating soln. contg. CrO3 and H2SO4 at 80A/dm<2> and further the steel sheet as an anode is subjected to the reverse electrolytic treatment for 0.2sed at 3.5A/dm<2> and is then immersed in a plating soln. contg. CrO3 and is electrolytically treated with the Cr acid by the cathodic treatment at 10 Coulomb/dm<2> quantity of electricity. The steel sheet is cathodically treated for the cathodic treatment and is used as the electrode for the reverse electrolysis for the anodic treatment in the electrode for the reverse electrolysis for the cathodic treatment, by which the uniform Cr oxide film is formed and the tin-free steel having the stable quality is produced.

Description

【発明の詳細な説明】 本発明は、鋼板の表面に金属クロムの下層と、クロム水
利酸化物の上層とを有するティンフリー鋼板、特に接着
缶用として耐レトルト処理性ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a tin-free steel plate having a lower layer of metallic chromium and an upper layer of chromium water-containing oxide on the surface of the steel plate, particularly a retort-resistant steel plate for adhesive cans.

〈従来技術とその問題点〉 最近、電解クロメート処理鋼板は、ティンフリースチー
ルクロムタイプ(以下TFSと略称する)と称され、ブ
リキに代る缶用材料としての特性が認められ、内容物の
充填が低温状態でなされる低温パックのみならず内容物
を高温殺菌して充填するいわゆるホットバック用または
パック後高温で殺菌処理を行うレトルト処理が必要とさ
れる缶用材料へと用途も拡大されるようになった。
<Prior art and its problems> Recently, electrolytic chromate-treated steel sheets, called tin-free steel chromium type (hereinafter abbreviated as TFS), have been recognized for their properties as a material for cans that can replace tinplate. Applications are expanding not only to low-temperature packs, where the contents are sterilized at low temperatures, but also to so-called hot bags, in which the contents are sterilized at high temperatures before being filled, and can materials, which require retort processing, in which sterilization is performed at high temperatures after packaging. It became so.

この用途が拡大されることにより、TFSは一般にその
製缶に当っては缶胴はポリアミド系接着剤で接合されて
いるため缶胴が破れるという問題が発生している。
With the expansion of this use, the problem has arisen that when TFS is manufactured into cans, the can body is generally bonded with a polyamide adhesive, which causes the can body to break.

接着毎における缶胴の破れは、塗膜−TFS界面から剥
離することにより起こるもので、塗膜とTFSとの界面
の密着性が低下することは、従来からクロムめっき浴、
電解クロム浴に添加されていた硫酸の水和酸化クロム被
膜中への共析によりWtt−1411cif!+−一に
、+−に*1.1τソ’xNi&+)tFIl、b−*
浴に添加しない方法等が提案されている。しかし、硫酸
を添加しないクロムめっき浴では、めっき効率が低く、
製造効率の低下や、安定したクロムめっきが行われない
ため、品質安定性の上から好ましくなく、工業的には多
くの問題点が残っていた。
The tearing of the can body after each adhesion occurs due to peeling from the paint film-TFS interface, and the decrease in adhesion between the paint film and TFS has traditionally been caused by chromium plating baths,
Wtt-1411cif! by eutectoiding of sulfuric acid added to the electrolytic chromium bath into the hydrated chromium oxide film! +-1, +-*1.1τso'xNi&+)tFIl, b-*
Methods that do not add it to the bath have been proposed. However, chromium plating baths without sulfuric acid have low plating efficiency.
This method is unfavorable in terms of quality stability, as it reduces production efficiency and does not provide stable chromium plating, and many problems remain from an industrial perspective.

そこで、これらの欠点を解決する方法としてクロムめっ
き後にクロム酸水溶液中で鋼板を陽極とする逆電解を施
し、その後にクロム酸水溶液中で電解クロム酸処理を施
すことが提案されている(特願昭5.6−62766号
参照)。
Therefore, as a method to solve these drawbacks, it has been proposed to perform reverse electrolysis using the steel plate as an anode in an aqueous chromic acid solution after chromium plating, and then to perform electrolytic chromic acid treatment in an aqueous chromic acid solution (patent application). (See No. 5.6-62766).

しかし、クロムめっき工程と、電解クロム酸処理工程と
の間に、鋼板を陽極処理として連続的に逆電解を施した
場合、逆電解用電極があるクロム浴中の浴電圧が上昇し
、逆電解用電極表面上での金属クロムの析出および水素
ガスの発生を引き起こし、逆電解処理が不均一となり、
逆電解処理による効果が十分に発揮されなくなる。さら
に、逆電解処理による効果が不十分であると、めっき後
に鋼板を陽極として施す逆電解処理によって鋼板表面層
の性質が変り、その後の電解クロム酸処理におけるクロ
ム水和酸化物被膜の形成に影響を及ぼし、クロム水和酸
化物被膜が不均一に形成され、製品の品質安定性の低下
をもたらすことがある。
However, when reverse electrolysis is applied continuously to the steel plate as an anodizing process between the chromium plating process and the electrolytic chromic acid treatment process, the bath voltage in the chromium bath where the reverse electrolysis electrode is located increases, and the reverse electrolysis This causes the precipitation of metallic chromium and the generation of hydrogen gas on the surface of the electrode, making the reverse electrolytic treatment uneven.
The effect of reverse electrolytic treatment will not be fully exerted. Furthermore, if the effect of reverse electrolytic treatment is insufficient, the properties of the surface layer of the steel sheet will change due to the reverse electrolytic treatment applied after plating, using the steel sheet as an anode, and this will affect the formation of a chromium hydrated oxide film in the subsequent electrolytic chromic acid treatment. This may cause a chromium hydrated oxide film to be formed non-uniformly, leading to a decrease in product quality stability.

〈発明の目的〉 本発明は、陽極処理用としての逆電解用電極に高価な金
および白金等の電極を用いることなく、鋼板への逆電解
処理を効果的に施すための方法としてクロムめっき後該
液中で鋼板を陽極処理とした逆電解処理を含むクロムめ
っき処理−逆電解処理−電解クロム酸処理工程を行う前
に、逆電解処理用電極において陰極処理を数時間施して
から。
<Purpose of the Invention> The present invention provides a method for effectively applying reverse electrolytic treatment to a steel plate without using expensive gold or platinum electrodes for reverse electrolytic treatment for anodizing after chromium plating. Before carrying out the chromium plating process including reverse electrolytic treatment in which the steel plate is anodized in the solution - reverse electrolytic treatment - electrolytic chromic acid treatment, cathodic treatment is performed for several hours at the electrode for reverse electrolytic treatment.

陽極処理用電極として用いる事によりクロム水和酸化物
被膜を均一に形成することができるレトルト缶用ティン
フリースチールの製造方法を提供することを目的とする
An object of the present invention is to provide a method for manufacturing tin-free steel for retort cans, which can uniformly form a chromium hydrated oxide film by using it as an electrode for anodizing.

〈発明の構成〉 本発明は、クロムを含有する水溶液中で薄鋼板に陰極処
理することによって金属クロムを主体とする電気めっき
を行い、引きつづき該溶液中で、陽極処理を施し、その
後にさらにクロムを含有する水溶液中で電解クロム酸処
理を行うことにより、耐レトルト処理性に優れたティン
フリスチールを製造するにあたり、前記陽極処理に用い
る電極において予め陰極処理を施してから、陽極処理用
電極として用いることを特徴とするレトルト缶用ティン
フリスチールの製造方法を提供するものである。
<Structure of the Invention> The present invention performs electroplating mainly consisting of metallic chromium by cathodic treatment of a thin steel plate in an aqueous solution containing chromium, followed by anodization in the solution, and then further plating. In order to produce tin-free steel with excellent retort resistance by performing electrolytic chromic acid treatment in an aqueous solution containing chromium, the electrodes used for anodizing are first cathodized, and then the electrodes for anodizing are The present invention provides a method for manufacturing tin-free steel for retort cans, which is characterized in that it is used as a retort can.

以下、本発明をさらに詳細に説明する。The present invention will be explained in more detail below.

本発明によれば、鋼板を陽極とした逆電解処理を用いた
工程によりティンフリースチールを製造するにあたり、
予め逆電解処理用電極において鋼板を陰極とした陰極処
理を施し、電極性状を安定化させてから、該工程を行い
、薄鋼板に片面50〜200 mg/m2の金属クロム
めっきを施し、この金属クロム層表面に5〜30 mg
/m2のクロム水和酸化物被膜を形成したTFSを得よ
うとするものである。
According to the present invention, tin-free steel is manufactured by a process using reverse electrolytic treatment using a steel plate as an anode.
In advance, cathode treatment is performed using a steel plate as a cathode in an electrode for reverse electrolytic treatment to stabilize the electrode properties, and then this process is performed, and one side of the thin steel plate is plated with metal chromium at a concentration of 50 to 200 mg/m2, and this metal 5 to 30 mg on the surface of the chromium layer
The objective is to obtain a TFS in which a chromium hydrated oxide film of /m2 is formed.

す、200 mg/ra2を越えても耐食性の向上は望
めないので通常のTFSは50〜200mg/s2 (
7)金属クロムを有している。
Even if it exceeds 200 mg/ra2, no improvement in corrosion resistance can be expected, so normal TFS is 50 to 200 mg/s2 (
7) Contains metallic chromium.

一方、クロム水利酸化物被膜が5mg/112未満では
所望の塗料密着性が得られず、また3 0 mg/m2
を越えると外観が悪くなったり、加工時にクロム水利酸
化膜にクラックが入って実用的でない。
On the other hand, if the amount of chromium water-conserving oxide film is less than 5 mg/112, the desired paint adhesion cannot be obtained;
Exceeding this value may result in poor appearance or cracks in the chromium water-retaining oxide film during processing, making it impractical.

通常、クロムめっき液中で、鋼板を陽極とした逆電解処
理を例えば鉛系のアノードで実施した場合、電気抵抗の
大きい黄色のスケール(PbCrO2)が電極表面上に
形成され、アノードの通電性が悪化される。スケールの
生成により通電性が悪化されることにより、逆電解処理
が不均一となる。
Normally, when reverse electrolytic treatment is performed in a chromium plating solution using a steel plate as an anode, for example with a lead-based anode, a yellow scale (PbCrO2) with high electrical resistance is formed on the electrode surface, reducing the electrical conductivity of the anode. It gets worse. The generation of scale impairs electrical conductivity, resulting in non-uniform reverse electrolytic treatment.

また、このスケールは、電極表面に生じてボロボロにな
って落ちる程、電極を腐食し、電極と鋼板との極間距離
を不安定にさせるものである。
Further, this scale forms on the electrode surface and corrodes the electrode to the extent that it crumbles and falls off, making the distance between the electrode and the steel plate unstable.

そこで1本発明は、スケール(PbCr02 )が電極
表面上に形成される前に陰極処理により7ノ一ド表面に
通電性が良く硬く緻密な二酸化鉛(pbo2 )ケール
の生成を極めて少なくすることを提供することにある。
Therefore, one aspect of the present invention is to minimize the formation of lead dioxide (pbo2) scale, which has good electrical conductivity and is hard and dense, on the node surface by cathodic treatment before scale (PbCr02) is formed on the electrode surface. It is about providing.

このようにして逆電解用電極の腐食を防ぐことにより、
逆電解処理の効果が均一となり、安定したクロム水利酸
化物被膜の形成を促し、耐レトルト処理性に優れたティ
ンフリースチールを製造することができる。
By preventing corrosion of the reverse electrolysis electrode in this way,
The effect of the reverse electrolytic treatment becomes uniform, promoting the formation of a stable chromium water-retaining oxide film, and making it possible to produce tin-free steel with excellent retort treatment resistance.

〈実施例〉 以下、本発明を実施例につき具体的に説明する。<Example> Hereinafter, the present invention will be specifically explained with reference to examples.

(1)逆電解用電極における陰極処理 逆電解処理用電極においてクロム酸水溶液中で7 A/
dm2の電流密度で鋼板を陰極としての陰極処理を1時
間行った。
(1) Cathode treatment in the electrode for reverse electrolysis treatment in the chromic acid aqueous solution in the electrode for reverse electrolysis treatment at 7 A/
Cathode treatment was performed for 1 hour using a steel plate as a cathode at a current density of dm2.

引き続き板厚0.22mmの冷延鋼板(T4−CA)を
5%NaOH溶液で70℃、8 A/dm2 (7)電
流密度で10秒間の電解脱脂を行い、水洗後、3%H2
SO4中に5秒間浸漬し、水洗した後、鋼板に対して下
記の処理を行った。
Subsequently, a cold-rolled steel plate (T4-CA) with a thickness of 0.22 mm was electrolytically degreased with a 5% NaOH solution at 70°C at a current density of 8 A/dm2 (7) for 10 seconds, and after washing with water, it was degreased with 3% H2
After immersing in SO4 for 5 seconds and washing with water, the steel plate was subjected to the following treatment.

(2)クロムめっき処理 めっき液組成 CrO:+ 180  gel 液温5
0℃H2SO40,75g/ I Ha2SiF68  gel めっき条件 電流密度80 A/da2で1.2秒間陰
極処理を行った。
(2) Chromium plating treatment plating solution composition CrO: + 180 gel Solution temperature 5
0°C H2SO40, 75g/I Ha2SiF68 gel Plating conditions: Cathode treatment was performed at a current density of 80 A/da2 for 1.2 seconds.

(3)逆電解処理 鋼板を陽極として3.5 A/dm2 、0.2秒の逆
電解処理を行った。
(3) Reverse electrolytic treatment A reverse electrolytic treatment was performed at 3.5 A/dm2 for 0.2 seconds using the steel plate as an anode.

(4)電解クロム酸処理 めっき液組成 CrO3Go gel  液温50℃N
a25iFa 5tag/!;L めっき条件 10クーロン/d112の電気量で陰極処
理を行った。
(4) Electrolytic chromic acid treatment plating solution composition CrO3Go gel Solution temperature 50℃N
a25iFa 5tag/! ;L Plating conditions: Cathode treatment was performed with an amount of electricity of 10 coulombs/d112.

前述の(1)の逆電解用電極を用いて鋼板を陰極処理す
る処理を施した場合(発明例)と施さない場合(比較例
)について、上記の(2)クロムめっき処理、(3)逆
電解処理、(4)電解クロム酸処理を組み合せてTFS
を製造し、蛍光X線により分析したクロム水利酸化物被
膜量の板巾方向でのばらつきの経時変化を第1図に示す
Regarding the case where the steel plate is subjected to the cathodic treatment using the reverse electrolysis electrode of (1) above (invention example) and the case where it is not applied (comparative example), the above (2) chromium plating treatment, (3) reverse TFS by combining electrolytic treatment and (4) electrolytic chromic acid treatment.
Figure 1 shows the variation over time in the amount of chromium water-retaining oxide coating in the width direction of the plate, which was analyzed using fluorescent X-rays.

以上、本発明の効果は第1図の実施例を通じて明らかに
された通り鋼板を陽極処理用としての逆電解用電極にお
いて予め鋼板を陰極処理用として陰極処理を施してから
、鋼板を陽極処理とした逆電解用電極として用いること
により均一なりロム酸化物被膜が形成され、製品の品質
安定性を確保することができる。
As mentioned above, the effects of the present invention are as clarified through the embodiment shown in FIG. By using it as an electrode for reverse electrolysis, a uniform chromium oxide film is formed, and the quality stability of the product can be ensured.

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

第1図は通電条件を一定とした場合の板巾方向でのクロ
ム水和酸化物被膜量のばらつきの経時変化を示すグラフ
である。 二二・・、( オし1 yt:: − 司r M、l、。 FIG、1 使用端間(H「) 甲
FIG. 1 is a graph showing the variation over time in the amount of chromium hydrated oxide coating in the width direction of the plate under constant current supply conditions. 22..., (Oshi1 yt:: - Tsukasa r M, l,. FIG, 1 Between the ends of use (H") A

Claims (1)

【特許請求の範囲】[Claims] クロムを含有する水溶液中で薄鋼板に陰極処理すること
によって金属クロムを主体とする電気めっきを行い、引
きつづき該溶液中で、陽極処理を施し、その後にさらに
クロムを含有する水溶液中で電解クロム酸処理を行うこ
とにより、耐レトルト処理性に優れたティンフリスチー
ルを製造するにあたり、前記陽極処理に用いる電極にお
いて予め陰極処理を施してから、陽極処理用電極として
用いることを特徴とするレトルト缶用ティンフリスチー
ルの製造方法。
Electroplating consisting mainly of metallic chromium is performed by cathodic treatment of a thin steel plate in an aqueous solution containing chromium, followed by anodization in the solution, and then electroplating of chromium in an aqueous solution containing chromium. A retort can characterized in that, in producing tin-free steel with excellent retort treatment resistance by acid treatment, the electrode used for anodization is previously subjected to cathode treatment and then used as an electrode for anodization. Manufacturing method for tin-free steel.
JP10467385A 1985-05-16 1985-05-16 Production of tin-free steel for retort can Granted JPS61264195A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10467385A JPS61264195A (en) 1985-05-16 1985-05-16 Production of tin-free steel for retort can

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10467385A JPS61264195A (en) 1985-05-16 1985-05-16 Production of tin-free steel for retort can

Publications (2)

Publication Number Publication Date
JPS61264195A true JPS61264195A (en) 1986-11-22
JPH0421759B2 JPH0421759B2 (en) 1992-04-13

Family

ID=14386987

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10467385A Granted JPS61264195A (en) 1985-05-16 1985-05-16 Production of tin-free steel for retort can

Country Status (1)

Country Link
JP (1) JPS61264195A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022092815A (en) * 2020-12-11 2022-06-23 Jfeスチール株式会社 Steel sheet for cans and production method thereof

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61250195A (en) * 1985-04-27 1986-11-07 Nippon Steel Corp Manufacture of electrolytically chromated steel sheet having superior adhesion to paint

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61250195A (en) * 1985-04-27 1986-11-07 Nippon Steel Corp Manufacture of electrolytically chromated steel sheet having superior adhesion to paint

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022092815A (en) * 2020-12-11 2022-06-23 Jfeスチール株式会社 Steel sheet for cans and production method thereof

Also Published As

Publication number Publication date
JPH0421759B2 (en) 1992-04-13

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