JPH0570996A - Production of tin-free steel plate - Google Patents

Production of tin-free steel plate

Info

Publication number
JPH0570996A
JPH0570996A JP23318091A JP23318091A JPH0570996A JP H0570996 A JPH0570996 A JP H0570996A JP 23318091 A JP23318091 A JP 23318091A JP 23318091 A JP23318091 A JP 23318091A JP H0570996 A JPH0570996 A JP H0570996A
Authority
JP
Japan
Prior art keywords
electrolysis
steel plate
chromic acid
chromium
bath
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.)
Withdrawn
Application number
JP23318091A
Other languages
Japanese (ja)
Inventor
Toshio Sato
藤 利 夫 佐
Fumio Kokado
角 文 雄 古
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 JP23318091A priority Critical patent/JPH0570996A/en
Publication of JPH0570996A publication Critical patent/JPH0570996A/en
Withdrawn legal-status Critical Current

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  • Electroplating Methods And Accessories (AREA)

Abstract

PURPOSE:To provide the process for production of the TFS steel which has excellent secondary adhesion of a coating material and has color tones uniform even in the transverse direction of a strip. CONSTITUTION:This process consists in continuous production of the tin free steel plate by subjecting the steel plate to a cathodic electrolysis in a chromium plating bath after degreasing and pickling to form metallic chromium and chromium oxide films, then subjecting the steel plate to a reverse electrolytic treatment in the same chrome plating bath, sufficiently rinsing the steel plate and, succession, subjecting the steel plate to the cathodic electrolysis in an electrolytic chromic acid treating bath to form the chromium oxide films. The steel plate is subjected to the initial electrolysis by alternating currents consisting of the continuous repetition of the anodic electrolysis and the cathodic electrolysis in the above-mentioned electrolytic chromic acid treating bath before the execution of the cathodic electrolysis in the electrolytic chromic acid treating bath.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、塗料二次密着性に優
れ、且つ、均一な外観を有するティンフリー鋼板を製造
する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a tin-free steel sheet which is excellent in secondary adhesion of paint and has a uniform appearance.

【0002】[0002]

【従来の技術】ティンフリー鋼板(以下TFSと称す)
を缶胴として使用する缶の、缶胴を接合する方法のひと
つとして接着剤を用いて接合する方法(接着法)が普及
したが、用途の拡大にともない、TFSの塗料二次密着
性の向上に対する要求が増大した。これらの要求に対
し、多くのTFSの製造法が検討されてきた。その中で
も特開昭57−177998号「TFSの製造方法」
(逆電解法)は優れたものである。この逆電解法は、ク
ロムめっき浴中でクロムめっき後、同浴中で直ちに逆電
解し、水洗後、電解クロム酸処理浴中で、クロム酸化膜
を形成させることにより優れた塗料二次密着性を有する
TFSが製造できる。
2. Description of the Related Art Tin-free steel plate (hereinafter referred to as TFS)
As a method of joining the can bodies of cans that use as a can body, a method of joining with an adhesive (adhesion method) has become widespread, but with the expansion of applications, the secondary adhesion of TFS paint is improved. The demand for was increased. Many TFS manufacturing methods have been investigated to meet these requirements. Among them, JP-A-57-177998 "TFS production method"
(Reverse electrolysis method) is excellent. This reverse electrolysis method provides excellent secondary coating adhesion by forming a chromium oxide film in the electrolytic chromic acid treatment bath after chrome plating in the chrome plating bath, followed by immediate reverse electrolysis in the same bath, washing with water. Can be produced.

【0003】[0003]

【発明が解決しようとする課題】このような逆電解法に
よるTFSの製造において、逆電解処理したあとで電解
クロム酸処理浴中でそのまま陰極処理を行うとストリッ
プ(鋼帯)の幅方向でエッジより50mmまでの色調
と、ストリップセンター部の色調が異なるという問題が
あった。
In the production of TFS by such a reverse electrolysis method, if the cathodic treatment is carried out as it is in the electrolytic chromic acid treatment bath after the reverse electrolysis treatment, the edge in the width direction of the strip (steel strip) is obtained. There is a problem that the color tone up to 50 mm is different from the color tone of the strip center portion.

【0004】[0004]

【発明の目的】かくして本発明の目的は、塗料二次密着
性に優れ、しかもストリップ幅方向でも均一な色調を有
するTFSの製造方法を提供することにある。
SUMMARY OF THE INVENTION It is, therefore, an object of the present invention to provide a method for producing a TFS having excellent secondary adhesion of a paint and having a uniform color tone in the strip width direction.

【0005】[0005]

【発明の概要および詳細】すなわち、本発明によれば、
鋼板を脱脂、酸洗してからクロムめっき浴中で陰極電解
して金属クロムとクロム酸化膜を形成した後、引き続き
同じクロムめっき浴中で逆電解処理を行い、十分水洗
し、続けて、電解クロム酸処理浴中で陰極電解すること
により、クロム酸化膜を形成させるティンフリー鋼板を
連続して製造する方法において、前記電解クロム酸処理
浴で陰極電解を行う前に、該電解クロム酸処理浴で鋼板
に対し、陽極電解と陰極電解の連続した繰り返しからな
る交番電流による初期電解を行うことを特徴とするティ
ンフリー鋼板(TFS)の製造方法が提供される。
SUMMARY OF THE INVENTION That is, according to the present invention,
After degreasing and pickling the steel sheet, and then performing cathodic electrolysis in a chromium plating bath to form metallic chromium and a chromium oxide film, subsequently perform reverse electrolysis treatment in the same chromium plating bath, thoroughly wash with water, and continue electrolysis. A method for continuously producing a tin-free steel sheet for forming a chromium oxide film by performing cathodic electrolysis in a chromic acid treatment bath, wherein the electrolytic chromic acid treatment bath is used before cathodic electrolysis in the electrolytic chromic acid treatment bath. In the above, there is provided a method for producing a tin-free steel sheet (TFS), which comprises performing initial electrolysis on a steel sheet by an alternating current consisting of continuous repetition of anodic electrolysis and cathodic electrolysis.

【0006】本発明の方法で製造されるTFSは、通常
金属クロム20〜200mg/m2 、クロム酸化膜が金属ク
ロム換算で5〜50mg/m2 の範囲にあり、下層に金属ク
ロム、その上層にクロム酸化膜を有する二層構造を有
し、該鋼板は内外面となる面に缶用塗料を塗布した後、
ナイロン系の接着剤を介して缶胴を接着することにより
缶胴を形成し、缶胴の一方は、缶蓋が巻き締められてか
ら、食品などの内容物が80〜95℃の温度で熱間充填
(ホットパック)されるか、さらにその次工程として缶
胴を巻き締めて内容物を缶内に封じてから殺菌を目的と
して100℃以上の高温で加熱殺菌(レトルト処理)さ
れる缶の用途において上記のホットパックに引き続くレ
トルト処理後でも缶胴接合部の接着力が十分高く、TF
Sと塗料の間の密着力低下に起因する接着部の剥離(破
胴)を生じることがない、つまり塗料二次密着性に優れ
ると共にストリップ幅方向で均一な色調を有する。
[0006] TFS produced by the method of the present invention is usually metallic chromium 20 to 200 mg / m 2, chrome oxide layer is in a range of 5 to 50 mg / m 2 reckoned as metal chromium metal in the lower layer of chromium, the upper layer Has a two-layer structure having a chromium oxide film on the steel sheet, after applying a coating material for a can to the inner and outer surfaces,
The can body is formed by adhering the can body via a nylon-based adhesive, and one side of the can body is heated at a temperature of 80 to 95 ° C. after the contents of food and the like are closed after the can lid is wound. For cans that are either hot-packed or hot-packed as the next step, and then the contents are sealed in the cans by wrapping the can body and then heat sterilized (retort treatment) at a high temperature of 100 ° C or higher for sterilization. In the application, even after the retort treatment following the above hot pack, the adhesive strength of the can body joint is sufficiently high, and TF
No peeling (breakage) of the adhesive portion due to a decrease in adhesion between S and the paint, that is, excellent secondary adhesion of the paint and a uniform color tone in the strip width direction.

【0007】本発明を製造工程に従って具体的に説明す
る。冷延鋼板は脱脂、酸洗を経た後、クロムめっき浴中
で陰極電解され、不可避的に僅かな量のクロム酸化膜と
ともに金属クロムが析出する。クロムめっき浴はクロム
酸を主成分とし、更に金属クロムの析出効率を増すため
硫酸、弗化物または珪弗化物等の添加剤を適量添加した
通常の水溶液である。クロムめっき後、同じクロムめっ
き浴中で逆電解が直ちに実施される。逆電解は直流電源
あるいは交流電源を用いて行われ、鋼板上のクロム酸化
膜が除去される。
The present invention will be specifically described according to manufacturing steps. The cold-rolled steel sheet is degreased and pickled, and then subjected to cathodic electrolysis in a chromium plating bath, and metallic chromium is inevitably deposited together with a small amount of chromium oxide film. The chromium plating bath is a normal aqueous solution containing chromic acid as a main component and further containing an appropriate amount of an additive such as sulfuric acid, fluoride or silicofluoride in order to increase the deposition efficiency of metallic chromium. After chrome plating, reverse electrolysis is carried out immediately in the same chrome plating bath. Reverse electrolysis is performed using a DC power supply or an AC power supply, and the chromium oxide film on the steel plate is removed.

【0008】続いてドラグアウト槽、水洗槽を経由し
て、電解クロム酸処理槽へ入る。従来の方法によれば直
流電源で陰極電解されるが、本発明方法においては、図
1に示すような極性を異にする電流成分を有する電流
(広義の交流)を供給できる電源を用いて、直流電源に
よる陰極電解する前に初期電解を行う。
Subsequently, the electrolytic chromic acid treatment tank is entered through the dragout tank and the water washing tank. According to the conventional method, cathodic electrolysis is performed by a DC power source, but in the method of the present invention, a power source capable of supplying a current (AC in a broad sense) having current components having different polarities is used. Initial electrolysis is performed before cathodic electrolysis with a DC power supply.

【0009】このような初期電解でクロム酸化膜の生成
・除去をくり返し、緻密なクロム酸化膜を予めつくり引
き続き従来行われている陰極処理により、所望するクロ
ム酸化膜量を得る。ここで、この電解クロム酸処理浴は
クロム酸を主成分とし、クロム酸化膜の析出効率を増す
ための助剤として、硫酸、弗化物、珪弗化物等の添加剤
を加えた浴である。
The formation and removal of the chromium oxide film is repeated by such an initial electrolysis to form a dense chromium oxide film in advance, and the desired cathode oxide amount is obtained by the conventional cathode treatment. Here, the electrolytic chromic acid treatment bath is a bath containing chromic acid as a main component and an additive such as sulfuric acid, fluoride or silicofluoride added as an auxiliary agent for increasing the deposition efficiency of the chromium oxide film.

【0010】この極性を異にする電流は、鋼板の移動速
度(ライン スピード)と極板の長さによって決まる電
解時間内に、十分くり返される周期を有する交流である
ことが望ましく、実用上20msec以下の周期(図1
でt1 −t2 の値に相当)を持つ電流であれば十分効果
を有す。続いての次工程は水洗又は湯洗であり、その後
乾燥される。
The current having different polarities is preferably an alternating current having a cycle sufficiently repeated within an electrolysis time determined by the moving speed (line speed) of the steel plate and the length of the electrode plate, and is practically 20 msec. The following cycle (Fig. 1
And has a current corresponding to the value of t 1 -t 2 ). The subsequent next step is washing with water or washing with hot water, followed by drying.

【0011】このように製造されるTFSは、外観も均
一であり、塗料二次密着性も優れている。
The TFS thus produced has a uniform appearance and is excellent in the secondary adhesion of the paint.

【0012】なお、発明により幅方向の色調ムラが解消
される理由は定かではないが、いずれにしろクロム酸化
膜の生成・除去を繰り返すことにより生じる作用である
と考えられる。
Although the reason why the uneven color tone in the width direction is eliminated by the present invention is not clear, it is considered to be an action caused by repeating the generation and removal of the chromium oxide film in any case.

【0013】[0013]

【実施例】以下実施例および比較例により本発明をより
具体的に説明するが、以下の実施例、比較例においては
本発明によって得られたTFS(実施例1〜4)および
従来法によって得られたTFS(比較例1)を目視観察
によって色調の均一性を評価し、Tピール剥離試験によ
って塗料二次密着性の評価を行った。
The present invention will be described in more detail with reference to the following examples and comparative examples. In the following examples and comparative examples, the TFS (Examples 1 to 4) obtained according to the present invention and the conventional method were used. The obtained TFS (Comparative Example 1) was visually observed to evaluate the uniformity of color tone, and the T-peel peel test was performed to evaluate the secondary adhesion of the paint.

【0014】(実施例1〜4)板厚0.22mmの冷延
鋼板をラインスピード200mpmで連続して製造する
設備で85℃で5%NaOH溶液中、10A/dm2の電流密度
で、10秒間電解脱脂を行ってから水洗し、35℃の1
0%H2SO4 中に4秒間浸漬して、水洗した後に次の条件
でクロムめっきおよび逆電解処理を行った。クロムめっき処理条件 浴組成 CrO3 200g/l+ H2SO4
g/l 浴温 50℃ 電解条件 50 A/dm2×1.0秒逆電解処理条件 2 A/dm2×0.5秒 上記のクロムめっき処理および逆電解処理後、水洗し、
直ちに次の条件で電解クロム酸処理を施した。電解クロム酸処理条件 浴組成 CrO3 60g/l+F- 0.1g
/l 浴温 40℃初期電解条件 鋼板に対する陽極実効電流密度 2 A/dm2(一定) 鋼板に対する陰極実効電流密度 0.1〜15 A/d
m2 電解時間 0.5秒陰極処理条件 7 A/dm2×1.0秒
(Examples 1 to 4) A cold rolled steel sheet having a thickness of 0.22 mm was continuously produced at a line speed of 200 mpm in a 5% NaOH solution at 85 ° C. at a current density of 10 A / dm 2 and 10 After electrolytic degreasing for 2 seconds, wash with water and
It was dipped in 0% H 2 SO 4 for 4 seconds, washed with water, and then subjected to chromium plating and reverse electrolysis under the following conditions. Chromium plating conditions Bath composition CrO 3 200 g / l + H 2 SO 4 2
g / l Bath temperature 50 ° C. Electrolysis conditions 50 A / dm 2 × 1.0 seconds Reverse electrolysis treatment conditions 2 A / dm 2 × 0.5 seconds After the above chromium plating treatment and reverse electrolysis treatment, washed with water,
Immediately, electrolytic chromic acid treatment was performed under the following conditions. Electrolytic Chromic Acid Treatment Conditions Bath Composition CrO 3 60g / l + F - 0.1g
/ L Bath temperature 40 ° C Initial electrolysis condition Anode effective current density for steel sheet 2 A / dm 2 (constant) Cathode effective current density for steel sheet 0.1-15 A / d
m 2 Electrolysis time 0.5 seconds Cathodic treatment condition 7 A / dm 2 × 1.0 seconds

【0015】(比較例1)実施例と同様にしてクロムめ
っきおよび逆電解をしたあとで初期電解を行わずに従来
の陰極処理を行った。但し陰極処理条件は10A/dm2×
1.0秒とした。その後水洗いし、実施例と同様の処理
をして、TFSを得た。
(Comparative Example 1) In the same manner as in Example 1, after performing chrome plating and reverse electrolysis, conventional cathode treatment was performed without initial electrolysis. However, the cathode treatment condition is 10 A / dm 2 ×
It was set to 1.0 second. Then, it was washed with water and treated in the same manner as in Example to obtain TFS.

【0016】本発明法によるTFS(実施例1〜4)お
よび従来法によるTFS(比較例1)の色調の均一性お
よび塗料二次密着性を調べた結果を表1に示す。これら
の結果より、本発明法によるTFSは板幅方向で色調の
差がなく均一な外観を有しており更に塗料二次密着性も
良好な結果を示すことが確認された。
Table 1 shows the results obtained by examining the uniformity of the color tone of the TFS according to the method of the present invention (Examples 1 to 4) and the conventional TFS (Comparative Example 1) and the secondary adhesion of the coating material. From these results, it was confirmed that the TFS according to the method of the present invention has a uniform appearance with no difference in color tone in the width direction of the plate and has a good secondary adhesion property of the coating.

【0017】 [0017]

【0018】[0018]

【発明の効果】本発明は、逆電解法によるTFS製造方
法において、めっき、逆電解後の電解クロム酸処理で初
期電解として、交番電流を用いることにより、板幅方向
で色調差のないTFSを安定的に製造できるようになっ
た。
INDUSTRIAL APPLICABILITY The present invention provides a TFS having no color difference in the plate width direction by using an alternating current as initial electrolysis in electrolytic chromic acid treatment after plating and reverse electrolysis in the method for producing TFS by the reverse electrolysis method. It became possible to manufacture stably.

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

【図1】本発明の電解クロム酸処理浴における初期電解
処理で使用される電流の波形の例を示すグラフである。
FIG. 1 is a graph showing an example of a waveform of a current used in an initial electrolytic treatment in an electrolytic chromic acid treatment bath of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】鋼板を脱脂、酸洗してからクロムめっき浴
中で陰極電解して金属クロムとクロム酸化膜を形成した
後、引き続き同じクロムめっき浴中で逆電解処理を行
い、十分水洗し、続けて、電解クロム酸処理浴中で陰極
電解することにより、クロム酸化膜を形成させるティン
フリー鋼板を連続して製造する方法において、前記電解
クロム酸処理浴で陰極電解を行う前に、該電解クロム酸
処理浴で鋼板に対し、陽極電解と陰極電解の連続した繰
り返しからなる交番電流による初期電解を行うことを特
徴とするティンフリー鋼板の製造方法。
1. A steel plate is degreased and pickled, and then cathodic electrolyzed in a chromium plating bath to form metallic chromium and a chromium oxide film, followed by reverse electrolysis in the same chromium plating bath, followed by thorough water washing. In a method for continuously producing a tin-free steel sheet for forming a chromium oxide film by continuously performing cathodic electrolysis in an electrolytic chromic acid treatment bath, before performing cathodic electrolysis in the electrolytic chromic acid treatment bath, A method for producing a tin-free steel sheet, which comprises performing initial electrolysis on a steel sheet in an electrolytic chromic acid treatment bath by alternating current consisting of continuous and repeated anodic electrolysis and cathodic electrolysis.
JP23318091A 1991-09-12 1991-09-12 Production of tin-free steel plate Withdrawn JPH0570996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23318091A JPH0570996A (en) 1991-09-12 1991-09-12 Production of tin-free steel plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23318091A JPH0570996A (en) 1991-09-12 1991-09-12 Production of tin-free steel plate

Publications (1)

Publication Number Publication Date
JPH0570996A true JPH0570996A (en) 1993-03-23

Family

ID=16950990

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23318091A Withdrawn JPH0570996A (en) 1991-09-12 1991-09-12 Production of tin-free steel plate

Country Status (1)

Country Link
JP (1) JPH0570996A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190141246A (en) * 2017-06-09 2019-12-23 제이에프이 스틸 가부시키가이샤 Steel plate for cans and manufacturing method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190141246A (en) * 2017-06-09 2019-12-23 제이에프이 스틸 가부시키가이샤 Steel plate for cans and manufacturing method thereof
CN110741110A (en) * 2017-06-09 2020-01-31 杰富意钢铁株式会社 Steel sheet for can and method for producing same
EP3617349A4 (en) * 2017-06-09 2020-03-18 JFE Steel Corporation Steel sheet for cans, and production method therefor
CN110741110B (en) * 2017-06-09 2022-02-25 杰富意钢铁株式会社 Steel sheet for can and method for producing same
US11339491B2 (en) 2017-06-09 2022-05-24 Jfe Steel Corporation Steel sheet for cans, and production method therefor

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Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 19981203