JPS60103200A - Tin-free steel having excellent adhesive properties - Google Patents

Tin-free steel having excellent adhesive properties

Info

Publication number
JPS60103200A
JPS60103200A JP21141583A JP21141583A JPS60103200A JP S60103200 A JPS60103200 A JP S60103200A JP 21141583 A JP21141583 A JP 21141583A JP 21141583 A JP21141583 A JP 21141583A JP S60103200 A JPS60103200 A JP S60103200A
Authority
JP
Japan
Prior art keywords
chromium
treatment
electrolytic
tin
reverse
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
JP21141583A
Other languages
Japanese (ja)
Other versions
JPS6234838B2 (en
Inventor
Toshiro Ichida
市田 敏郎
Hajime Ogata
緒方 一
Kyoko Yamaji
山地 京子
Shunichi Tsugawa
津川 俊一
Toshio Irie
敏夫 入江
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 JP21141583A priority Critical patent/JPS60103200A/en
Publication of JPS60103200A publication Critical patent/JPS60103200A/en
Publication of JPS6234838B2 publication Critical patent/JPS6234838B2/ja
Granted legal-status Critical Current

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  • Electrochemical Coating By Surface Reaction (AREA)

Abstract

PURPOSE:To obtain economically a tin-free steel having excellent resistance to retort treatment by specifying respectively the S/O value and the value of an alkali soluble component in a chromium hydroxide film in the stage of subjecting a steel sheet as an anode to a reverse electrolysis after Cr plating then further to an electrolytic chromic acid treatment. CONSTITUTION:A thin steel sheet is cathodically treated in an aq. soln. congt. Cr, for example, an aq. sulfuric acid soln. contg. CrO3, Na2SiF6, by which electroplating consisting essentially of metallic Cr is accomplished. The electroplated steel sheet as an anode is in succession thereto subjected to a reverse electrolytic treatment in an aq. soln. contg. Cr. The thin steel sheet after the reverse electrolytic treatment is subjected to an electrolytic chromic acid treatment in an aq. soln. contg. >=1 kind of CrO3, K2Cr2O7 and dichromate. The S/O in the hydrated chromic oxide film on the surface of the tin-free steel (TFS) obtd. in this case is regulated to >=1.8 and the alkali soluble component to >=30%, respectively, by which the TFS having extremely high adhesive properties is obtd.

Description

【発明の詳細な説明】 本発明は鋼板の表面上に金属クロムの下層と−クロム水
オl峡化物の上層とを有するティンフリースチール、特
に接着缶用の桐料として耐レトルト処理性にすぐれたW
、解りロメート処理鋼也に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides tin-free steel having a lower layer of metallic chromium and an upper layer of chromium-water ol-thorhombide on the surface of a steel plate, which has excellent retort treatment resistance, especially as a paulownia material for adhesive cans. W
, concerning Koriya mate-treated steel.

’tiL%/41クロメート処理鋼板はティンフリース
チル・クロムタイプ(以下、’r F Sと略称−「る
)と称され、ブリキに代る缶用材料としての9!f性が
酩められ、近年その使用量が増大している。T F S
は表向に金属クロムと水オugH化りロム被)IQをイ
jするため十分な溶接性能を持たず、その製缶に当って
は缶胴はエポキシ・フェノール系&J脂を塗装後、ナイ
ロン系接着剤で接合している。
'tiL%/41 chromate-treated steel sheet is called tin-free still chrome type (hereinafter abbreviated as 'rFS), and is known for its 9!f properties as a material for cans that can replace tinplate. Its usage has been increasing in recent years.T F S
The surface of the can body is coated with metal chromium and water UGH chromium), so it does not have sufficient welding performance because it has a high IQ, and when making cans, the can body is coated with epoxy, phenolic and J resin, and then nylon is used. It is joined with adhesive.

最近T F 8缶の用途が拡大し、炭1佼飲料やビール
など内容物の充填が低温状!法でなされるIJ−(温バ
ックのみならず、果汁およびコーヒーなどのように内容
物を旨温殺閑して充填するいわゆるポットパンク用また
はバック& +j”f>温で収酌処理ケ何うレトルト処
理が必要な缶にも使用されるようになって缶胴が破れる
トラブルが発生している。
Recently, the use of T F 8 cans has expanded, and the contents such as charcoal drinks and beer can be filled at low temperatures! IJ- (not only hot bags, but also so-called pot punk bags or bags in which contents such as fruit juice and coffee are heated and filled) As it has come to be used for cans that require retort processing, problems have arisen in which the can body breaks.

このホットパック、レトルト処理Vの除にT F S接
肩缶に生ずる缶胴の破れは、1jil記接合ff18の
ナイロン系接漸剤増を通して浸透する熱水により窪11
WとTFSとの界面の接着が恋< 7.cす、塗膜−1
’FS界面から剥離するために発生するものである。
The tear in the can body that occurs in the TFS shoulder can due to this hot pack and retort treatment is caused by the hot water penetrating through the nylon adhesive of the joint ff18.
Love the adhesion at the interface between W and TFS <7. c, coating film-1
'This occurs due to separation from the FS interface.

接着性のすぐれた′I″FSを得る目的で多くの研兇が
行われ、クロムめっき浴や゛1屏りロム眩浴に添加され
ている硫酸が水和ば化クロム被膜中に共析し、レトルト
処理時に溶出して塗IIA −’I’ F S界面剥離
を起すとの見解から、クロム水和岐化膜中に含まれる4
A威根を極力減らし、代ってフッ素イオンを用いた製品
(例えば、特公昭57−5344(1゜特開昭56−1
42897号参照)が多(提案されている。
In order to obtain ``I'' FS with excellent adhesion, a lot of research has been carried out, and the sulfuric acid added to the chromium plating bath or the chromium glare bath is eutectoid in the hydrated chromium film. , 4 contained in the chromium hydrated film is believed to be eluted during retort treatment and cause peeling at the coating IIA-'I' FS interface.
Products that use fluoride ions to reduce A-power as much as possible (for example, JP-A-57-5344 (1° JP-A-56-1)
42897) has been proposed.

しかし、そのためには、’I” F S最表面の水和ボ
化クロム膜を形成する亀屏りロム酸処理冶は勿論のこと
、クロムめっき浴にも硫酸を添加せず、代ってフッ素化
合物を添加する方法が採用されているが、その場合には
全組クロムの析出効率が悪く、製造能率を著しく低下さ
せたり、得られたTFSに表面汚れが多発して製品の品
寅安定性が急く、歩留りが劣り、工業的には多くの問題
が残っていたO 本願の発明者等は、この点を解消する方法としテ扛iシ
n ’l 言むクロムめつきγ在中でクロムめっキ後、
該液中で鋼板を陽極とする逆Fjj解を施し、その抜に
硫酸を添加しないクロム数水溶故中で屯珀クロム酸処理
を施すことを提案し−fc (i)ケ開11tJ 57
−277998号参照)。しかし、そ(/’)俵の調査
によって、クロムめっき工程と’it 14クロム酸処
理工桿どの間に鋼&を陽極として逆*酵を施す工程を押
入するこの方法は、塗料密着性の改善に欅めC4i効で
あるが、逆電)ψト後の鋼板においては、その後の電解
クロム醒処理工程でのクロム水A11 酸化膜の成長が
抑制され、すぐれた塗料密〃i性ケ示−1−’l’E’
sを安定して得るため九は、喝7’jlクロム酢処理工
程で多量の′1b、気血を必要とし、経済的′1:ない
ことか判明した、 本発明は上述したような状況に珀みてなされたもので、
経済的に効率良(製造でき、しかも耐レトルト処理性の
極めて丁ぐれた′1゛P′Sを提供することを目的とす
る。
However, in order to do this, it was necessary not only to add sulfuric acid to the chromium plating bath, but also to add fluorine to the chromium plating bath. A method of adding a compound has been adopted, but in this case, the precipitation efficiency of all the chromium compounds is poor, resulting in a significant decrease in manufacturing efficiency, and the resulting TFS has frequent surface stains, which impairs the quality of the product. However, the inventors of the present application devised a method to solve this problem, which is called chromium plating in γ. After plating,
We proposed to perform a reverse FJJ solution using a steel plate as an anode in the solution, and to perform a chromic acid treatment in an aqueous chromium solution without adding sulfuric acid.
-277998). However, after investigating the bales, it was discovered that this method of inserting a reverse fermentation process using steel as an anode between the chromium plating process and the chromic acid treatment process improved paint adhesion. Although C4i has a strong C4i effect, the growth of chromium water A11 oxide film in the subsequent electrolytic chromium cleaning process is suppressed in the steel plate after reverse electrostatic discharge, showing excellent paint adhesion. 1-'l'E'
In order to stably obtain s, a large amount of chlorine and blood is required in the chromium vinegar treatment process, and it has been found that it is not economical.The present invention solves the above-mentioned situation. It was done after seeing a lot of things,
The object of the present invention is to provide a '1'P'S that can be produced economically and efficiently and has extremely good retort resistance.

本発明は薄鋼板に片IIIJ50〜200■/dの金属
クロムめっきを施し、該金属クロム増表面に5〜30〜
/dのクロム水和度化物被膜を有するTFSK関するも
のである、金属クロム層は50〜1rrl未7−では耐
食性が劣ってよ(ない。また2、00〜/、7より多く
ても耐食性の更なる向上は望めないので、通常のTFS
は50〜200 +v/ 、1の金属クロム層を有して
いる。−力、クロム水和酸化物被膜が5Tη/ゼ未滴で
は所望の塗料密層性が得られず、また3 0 Mf /
 yrlより多いと外観が悪くなったり、加工時にクロ
ム水第U酸化物被膜にクラックが入って実用的でない。
In the present invention, metal chromium plating is applied to a thin steel plate at a thickness of 50 to 200 cm/d, and the metal chromium-enhanced surface is coated with 5 to 30 μm/d.
Regarding TFSK with a chromium hydrate coating of /d, the metallic chromium layer has poor corrosion resistance at less than 50~1rrl. Since further improvement cannot be expected, normal TFS
has a metallic chromium layer of 50-200 +v/1. - If the chromium hydrated oxide film has a droplet of 5 Tη/ze, the desired paint layer density cannot be obtained;
If the amount is more than yrl, the appearance will deteriorate and the chromium water U oxide film will crack during processing, making it impractical.

更にいえば、クロム水滓1」敵化物被1模知は8〜25
η/dが最も望ましい。
Furthermore, chromium slag 1" enemy monster hit 1 knowledge is 8-25
η/d is most desirable.

本願の発明者等は先に塗料密着性にすぐれたTFSの製
造方法として、硫酸を添加したクロムめっき浴でクロム
めっき後、該液中で鋼板を陽4―とする逆電解を施し、
次いで硫酸を會まないクロム酸水溶液中で電解クロム酸
処理を施すことを提案した(+!j開昭57−1779
98号参照)。その故の調査のM朱、クロムめっき工程
と゛屯屏クロム酸処理工程との間に鋼板火陽極として逆
電解な施す工程を挿入するこの方法は、塗料VB層性の
よいTFS製造に有効であるが、逆電解後の鋼板におい
ては、その後の電解クロム酸処理工程でのクロム水利酸
化物膜の成長が抑制され、すぐれた萌科密漸性を示すT
FSを安定して44)るためには、電解クロム削処理工
程で多量の電気)11.乞必要とし、経済的でないこと
が判明した、この原因については定かでないが、クロム
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
板表面層の性質が袈ったためと思われる。
The inventors of the present application previously proposed a method for producing TFS with excellent paint adhesion, by chromium plating in a chromium plating bath to which sulfuric acid was added, and then performing reverse electrolysis to make the steel plate positive in the solution.
Next, he proposed electrolytic chromic acid treatment in an aqueous chromic acid solution without sulfuric acid (+!j Kaisho 57-1779).
(See No. 98). Therefore, this method of inserting a reverse electrolytic application process as a steel plate anode between the chromium plating process and the chromic acid treatment process is effective for producing TFS with good paint VB layer properties. However, in the steel sheet after reverse electrolysis, the growth of the chromium hydroxide film in the subsequent electrolytic chromic acid treatment process is suppressed, and the T.
In order to maintain stable FS44), a large amount of electricity is required in the electrolytic chromium cutting process11). The reason for this is not clear, but it is thought that the properties of the surface layer of the steel sheet were deteriorated by the reverse electrolytic treatment in which the steel sheet was used as an anode after chromium plating.

本願の元明者寺はこの逆電解によって変質したクロムめ
っき鋼板表面の特性にすa味を持ち、またTFSの塗料
缶層性VC関して、クロム水滓1」酸化物被膜中に共析
した硫酸根を肩書とする在来の説にも疑問を持って、ク
ロムめつき→通電テ昇→゛「1mクロム敵処理の工程を
社で製造した利先々の憾醒含−f4ttY有する’I”
 F Sについて、+m=Iレトルト処理性と水オ11
酸化クロム膜のS含南M、アルカリ”I rn分との関
係を定量的に調べた。その結果、クロムめつき→逆電解
→電解クロム酸処理の工程で袈mしたTFSにおいては
、水和酸化クロム膜中のS10≧0.18、アルカリ可
溶分≧30チのものは極めてすぐれた接着性が得られる
ことを見い出し、本発明を児成するに至ったものである
The Genmyojaji of this application has a taste in the characteristics of the surface of the chromium-plated steel plate that has been altered by this reverse electrolysis, and also has eutectoid properties in the chromium slag 1'' oxide film regarding the VC layer properties of the TFS paint can. I had doubts about the conventional theory that the sulfate root is the title, and chrome plating → energization → ``The frustration of the customers who manufactured the process of 1m chromium enemy treatment in the company-f4ttY has 'I''
For F S, +m=I retortability and water o11
We quantitatively investigated the relationship between the S content of the chromium oxide film and the alkali Irn content.As a result, it was found that hydration is It has been discovered that a chromium oxide film in which S10≧0.18 and alkali soluble content≧30 can provide extremely excellent adhesion, leading to the creation of the present invention.

TFSの品質特性な把握するために用いた耐レトルト処
理性の試験方法、水オIll”l!2化クコクロム膜中
10比およびアルカリ可溶分の測定方法は以下の辿りで
ある。
The test method for retorting resistance, the method for measuring the water-to-water ratio and the alkali-soluble content in the wolfberry chromium dioxide film, which were used to understand the quality characteristics of TFS, were as follows.

(1)酬レトルト処理性 ’r iL″Sの試料表面1にフェノール・エポキシ系
塗料を60 mf / drrl塗布し、210℃で1
2分間焼付けた。もう一つの試料表面2に同じ塗料を2
5my/dm’塗布し、同じ条件で焼付けた。この2つ
の試料を各々幅70m肩、長さ60藺に切断し、塗膜厚
の異なる2枚の試片の長さ方向の両端(IAおよび2 
A ) k 8 wだけ重ね、その曲に100μmnの
ナイロンフィルム3(接着剤)fK:はさみ、ホットプ
レスを用いて200℃で120秒の予熱を行った仮、3
 Kg/ criの加圧下で2()0℃で3()秒間の
用層を行った(第1a図参照)。この試験片4を10組
つくり、缶胴のように牛1そ1011 rrus程度に
予め丸めた後、底辺70rpxのアングル5に第lb図
に示すように固定し、125〜1 :3 (1℃、1.
6〜1.7 k、y /〜のレトルト釜中で300分経
時した時の剥)ill、の有無を訓べた。I O+hi
i中の剥1’i11本数で耐レトルト処理性の指標とC
7た。6・1−側力f去は以下の辿りである。
(1) Apply 60 mf/drrl of phenol-epoxy paint to the sample surface 1 of retort processable 'r iL''S, and apply it at 210℃ for 1 hour.
Bake for 2 minutes. Apply the same paint 2 to another sample surface 2.
It was applied at a rate of 5 my/dm' and baked under the same conditions. These two samples were each cut into pieces of 70 m wide and 60 m long, and two specimens with different coating thicknesses were cut at both ends in the length direction (IA and 2
A) Layer k 8 w and cover the song with 100 μm nylon film 3 (adhesive) fK: preheated at 200°C for 120 seconds using scissors and a hot press, 3
Layering was carried out at 2()0° C. for 3() seconds under a pressure of Kg/cri (see Figure 1a). Ten sets of these test pieces 4 were made, and after pre-rolling them to about 1011 rrus like a can body, they were fixed to an angle 5 with a base of 70 rpx as shown in Fig. , 1.
The presence or absence of peeling after 300 minutes in a retort pot of 6 to 1.7 k,y/~ was observed. IO+hi
The index of retort treatment resistance and C by the number of strips in i
7. 6.1-The lateral force f is traced as follows.

・・・・しl・ルト処理時のJd昆(L本数 (1/ 
1.0本へ・・・ 〃 1〜2/I(1本 ×・・・ 〃 3以上/10本 (21810比d(11定 i’ F Sの水和酸化クロムノ1曳中の(IQc I
蚊4ii!の3有Ikをオージェ電子分光法(Alas
と1晒称f)により調べ、第2図に示すようにAESチ
ャート」二〇敗素ビークと11ル黄ピークの強度比S1
0の値とじ−〔ボした、なお、AES副定は、真空度1
. OXl 0−9torr、 ビーム′屯圧10. 
OKVで1丁つ1.:。深さ方向の分析を行うため、A
1−スパッタを力1]I4・屯u= 4. o KV、
 山、流智度0.6μA/ trX、J’% S’−I
f 2.2 xlo−7torrで行った、ノ模中のS
 / 、0のI采さ方向の分布はM表面の少し内側(約
10にの深さ)で最大値をとる。本発明ではこの最大値
を各々の試料のS10値とした。
・・・Jdkon (L number (1/
To 1.0 lines...〃 1 to 2/I (1 line x... 〃 3 or more/10 lines (21810 ratio d (11 constant i' F
Mosquito 4ii! The three-dimensional Ik of
As shown in Figure 2, the intensity ratio of the 20 yellow peak and the 11 yellow peak on the AES chart is determined by
The value of 0 is set to 1.
.. OXl 0-9torr, beam pressure 10.
One by one at OKV. :. In order to perform depth analysis, A
1-sputtering force 1] I4・ton u= 4. o KV,
Mountain, flow rate 0.6μA/trX, J'% S'-I
f 2.2 S in the model conducted at xlo-7torr
/ , 0 in the I-shape direction takes its maximum value slightly inside the M surface (at a depth of about 10 mm). In the present invention, this maximum value was defined as the S10 value of each sample.

(3)アルカリ可溶分 子FSな210℃で12分間窒焼きした後、7、5 N
 −Na1l(により110 ℃で10分曲浸漬処理し
、その時に溶解したクロメート被1漠量をもとのクロメ
ート被膜量で割ったものである。11なの大きいものは
空焼きによってクロメート被膜が不溶化し難いこと馨示
す。
(3) Alkali-soluble molecule FS After nitriding at 210℃ for 12 minutes, 7.5N
- Na1l (110°C for 10 minutes), and the amount of chromate coating dissolved at that time was divided by the original amount of chromate coating. For those with a larger value of 11, the chromate coating was insolubilized by dry baking. I will show you something difficult.

本発明のT F Sの製造に際Cては、Yす鋼板を通常
の方法で置所脱脂、水洗後懺敵酸洸し、Cr0310(
)〜2 I) OP / l、 1(2S(J4 (1
5〜1t/l。
When manufacturing the TFS of the present invention, a Y steel plate is degreased in-situ using a conventional method, washed with water, and then dried in an acid bath to obtain Cr0310 (
)~2 I) OP/l, 1(2S(J4 (1
5-1t/l.

Na2SiF65〜8f/l の組成からなるクロムめ
っき浴中で陰極処理し、これにひきつづいてM?を中で
鋼板を陽極として0.3〜9ク一ロン/dm’の電気量
で逆電解処理を行い、水洗後無水りロム販:30〜9 
(l t/13,6tt酸0.03〜0.9 ill、
’t’lA’i加し℃調製した′m鮪クりム酸蔭中で鋼
板を陰極として処理した。
Cathodic treatment was performed in a chromium plating bath having a composition of 65 to 8 f/l Na2SiF, followed by M? Reverse electrolytic treatment is carried out using a steel plate as an anode with an electricity amount of 0.3 to 9 C/dm', and after washing with water, waterless ROM sales: 30 to 9
(l t/13,6tt acid 0.03-0.9ill,
The steel plate was treated as a cathode in a tuna cream acid solution prepared at 10°C.

得られた’r F Sの表面に形成された水和電化クロ
ム脱の量は、熱アルカリ水溶i (7,5N NaO,
Ii)での溶解作業前後の表面クロム句な蛍光X線分+
trによって検出し、d解h【を水AL1目支化クロム
i(tとした。
The amount of hydrated electrified chromium removed formed on the surface of the obtained 'r F S is determined by
Fluorescent X-ray segment of surface chromium before and after melting operation in Ii)
It was detected by tr, and the d-decomposition h was defined as water AL1 supported chromium i (t).

用いた試料はクロムめっきおよびm、1p(クロム岐処
理時の電気量をIi4整して金属クロム)1目」)0〜
120 thy/ m′、水*um化クロム量1o−2
0ノ〃y/ y(”のイ11囲に保たれていた。
The samples used were chromium plated, m, 1p (metallic chromium after adjusting the amount of electricity during chromium treatment with Ii4) 0~
120 thy/m', water * chromium content 1o-2
0ノ〃y/y(” was kept in the A11 box.

第3図にテストしたT F SO耐レしルト処理性乞、
水オIJ f’iグ化クロり族のS / f34匹」d
よびアルカリ可溶分の関係で示す。S10値か0.18
以上、アルカリ可溶分が30%以上の範囲にあるよう/
よ衣+(n破膜を翁するT h゛sでは、耐レトルト処
」11〕性が極めてすぐれていることがわかる。
Figure 3 shows the T FSO resistance resistance process tested.
Mizuo IJ f'i S / f 34 of the black tribe" d
and alkali soluble content. S10 value is 0.18
As mentioned above, the alkali soluble content is in the range of 30% or more/
It can be seen that the retort resistance (11) is extremely excellent in cases where membranes are ruptured.

以上の精米かも、クロムめつぎ汝胎板馨爾極として逆電
解処理を施した故、′屯h・「クロム版処理を行う方法
で製造されるl″FSにおいては、クロム水オロ酸化物
膜中のS / C1値が0.18以上、アルカリ可溶分
が30チ以上であれば塗イ→の重層性を極めて良好なレ
ベルに保つことができることが判明した。
Because the above rice milling process was reverse electrolyzed as a chrome plate, the chromium hydroxide film was It has been found that if the S/C1 value in the coating is 0.18 or more and the alkali soluble content is 30 or more, the multilayer property during coating can be maintained at an extremely good level.

従来発表された多くの研死結釆によれば、水イuば化ク
ロムに共伯した硫ば根は概してレトルト処理性を川うも
のとされ、また全焼処理時の水オロ酸化クロム膜の不溶
化しやすざの指標となるアルカ’J al浴分も商い値
はレトルト処理性を損うものとするのが通説であった。
According to many research results that have been published so far, the sulfur base that coexists with chromium hydroxide generally affects the retortability, and also contributes to the insolubilization of the chromium hydroxide film during burnout. It was a common belief that the Alka'J al bath content, which is an indicator of grain size, impairs retortability.

本発明は、クロムめっき工程と電解クロム酸処理工程と
の間に鋼板を陽極として処理する逆′tL W4工程を
採用した1゛P′Sにおいては、一定量以上の共4JT
 (Iff 酸根の存在がかえって耐レトルト処理性乞
向上させ、またレトルト処理汝の尚温1ml久性につい
ても従来に7よい良好な特性をイ1する製品を生み出す
ことを見出してなされた。その特性改善機構の詳細につ
いては足かでないが、クロムめっき後の逆電解処理によ
って鋼イル表]11の傳い水和酸化クロム膜が震質し、
その後の電解クロム散処理工程で硫酸を添加した処理浴
中で生成する、共析(mt咳根の多い、を焼処理時にア
ルカリ不溶化し難い膜の性賀に影響な与え、得もれた一
r P’ sの接層性を大幅に改善したものと考えられ
る。
In 1P'S, which uses a reverse 'tL W4 process in which a steel plate is treated as an anode between the chromium plating process and the electrolytic chromic acid treatment process, a certain amount or more of both 4JT
(Iff) It has been discovered that the presence of acidic radicals actually improves the retort resistance, and also produces a product that has better properties than the conventional one in terms of 1ml durability when retorted at still temperature. Although the details of the improvement mechanism are not clear, the reverse electrolytic treatment after chromium plating causes the hydrated chromium oxide film shown in Table 11 of the steel plate to become seismic.
During the subsequent electrolytic chromium dispersion treatment process, eutectoids (mt-rich), which are generated in the treatment bath to which sulfuric acid is added, have no effect on the performance of the film, which is difficult to insolubilize with alkali during the baking treatment, and the resulting It is considered that this greatly improves the contact properties of rP's.

υF本発明を実施例お1び比較例ケ挙げて44体的に説
明する。
υF The present invention will be specifically explained with reference to Examples and Comparative Examples.

板厚0.22關の凸月祇鋼伏(T4CA)をポメリ゛リ
ン浴故で80℃、15A/dm”の電υ1を密度で10
秒間の電解脱脂を行い、水洗後10%[2804中に5
秒間浸漬して水洗した後、下記の条件で本処理を行った
。本処理は、(1)クロムめっき工程→(2)逆電解処
理工程→(3)軍j弄りロム改処理IA′AのIll+
’tに竹い、(1)と(2)とは同一の′+44、)伜
液中で連続して実1Jluし、(2)と(3)の間およ
び(3)終了後には水洗をイエっだ。
A convex steel plate (T4CA) with a thickness of about 0.22 was heated at 80℃ in a pomerin bath, and with a density of 10
Electrolytic degreasing was performed for seconds, and after washing with water, 10% [5 in 2804]
After dipping for a second and washing with water, the main treatment was performed under the following conditions. This process consists of (1) chrome plating process → (2) reverse electrolytic treatment process → (3) army j tampering ROM modification treatment Ill+ of IA'A
't is bamboo, (1) and (2) are the same '+44,) 1 Jlu of fruit is continuously washed in the liquid, and between (2) and (3) and after (3) is finished, it is washed with water. No.

(1) クロムめっき めっき液組成 Cr(J3 150 f/eHzSO4
(1,3−1,Oy/(I Na2SiF6 7 t/11 めつき条件 液温50℃、rli−流V’j’j Ij
J451+ A/d m’で陰巾jv、処理 (2)逆電解処理 鋼板を陽極として0.5〜:4クーロン/ d m′の
逆電解処理を行った。比較のため逆電yjrを行わない
例も表1に示した。
(1) Chromium plating plating solution composition Cr(J3 150 f/eHzSO4
(1,3-1,Oy/(I Na2SiF6 7 t/11 Plating conditions Liquid temperature 50℃, rli flow V'j'j Ij
J451+ A/d m' with a shade width JV, Treatment (2) Reverse electrolytic treatment Reverse electrolytic treatment was performed at 0.5 to 4 coulombs/d m' using the steel plate as an anode. For comparison, Table 1 also shows an example in which reverse voltage yjr was not performed.

(3)1狂解クロム酸処理 組成 CrO360f/11 H2SU4 0.05〜0.6 f/lj液温 40〜
45℃ 硫醒炭度の異なるクロム敵浴中で陰極処理を何っだ。試
料即祠報にあたっては、クロムめっきおよび電解クロム
酸処理時の′也気是′f!r:調整して、金属クロム量
100〜2 o o my/ m、水1日酸化クロム量
10〜20■/1n°となるように処理した。得られた
試オ・1について測定した11σ・ルトルト処理性、水
オU酸化クロム1模のアルカリ可溶分、S/()値を表
1に示す。
(3) 1 Crazy chromic acid treatment composition CrO360f/11 H2SU4 0.05~0.6 f/lj liquid temperature 40~
What about cathodic treatment in chromium enemy baths with different sulfurization carbon degrees at 45℃? When reporting samples immediately, please be sure to check the conditions during chromium plating and electrolytic chromic acid treatment. r: The amount of metal chromium was adjusted to be 100 to 2 o omy/m, and the amount of chromium oxide per day in water was 10 to 20 μ/1n°. Table 1 shows the 11σ retort processability, the alkali soluble content of water-based chromium oxide 1, and the S/() value measured for the obtained sample O-1.

表1の結果から、(1)クロムめつぎ→(2)逆電解→
(3)電解りロム酵処理の工程で製造したl’ FSに
おいては、表面の水和ば化クロム(模がS / o≧0
.18のS馨せみ、アルカリd■溶分30チ以上であれ
ば、耐レトルト処理性が極めて良好なことがわかる。
From the results in Table 1, (1) Chrome Metsugi → (2) Reverse electrolysis →
(3) In l' FS produced in the process of electrolytic ROM fermentation treatment, hydrated chromium on the surface (S/o≧0
.. It can be seen that retort treatment resistance is extremely good if the S value of 18 and the alkali d soluble content is 30 or more.

逆′It購処理を行う同様な工程で処理されたTFSで
あっても、S/()値、アルカリrJTY6分力・上i
己の領域を満足しない場合には不十分な特性となってい
る。また、逆電解処理を行わない場合には、=られたi
’ F Sの水和酸化クロム族がS / Of@、アル
カリ可溶分に関して上記の領域を満足しても、著しく劣
った塗料密看性しか示さない。
Even for TFS processed in a similar process using reverse 'It purchasing processing, the S/() value, alkali rJTY6 component force, upper i
If you are not satisfied with your own area, it is an insufficient characteristic. In addition, when the reverse electrolytic treatment is not performed, the i
Even if the hydrated chromium oxide group of FS satisfies the above range with respect to S/Of@, alkali soluble content, it exhibits significantly poor paint tightness.

表1Table 1

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

第1図はrlI′Sの塗料@瘤力の耐レトルト処理性試
験方法の概賛図、第2図はAES測定チャート図、第3
図はTFSの耐レトルト処理性と水オMY化クロム膜の
S10値およびアルカリMJ浴分との関係をボすグラフ
である。 第2図 E (eV) 萬3図 アルカリ可溶分
Figure 1 is a schematic diagram of the retort resistance test method for rlI'S paint @ lump force, Figure 2 is an AES measurement chart, and Figure 3
The figure is a graph showing the relationship between the retort treatment resistance of TFS, the S10 value of the water-omylated chromium film, and the alkaline MJ bath content. Figure 2 E (eV) Figure 3 Alkali soluble content

Claims (1)

【特許請求の範囲】[Claims] クロムを含有する水溶液中で薄5IIIIl板を陰極処
理して金属クロムを主体とする電気めっきを行い、ひき
つづきクロムを含有する水76液中で鋼板を陽極として
逆電解処理を施した後に、無水クロム酸、重クロム酸お
よび重クロム塩酸よりなる!IPから選んだ1 at以
上を含有する水溶液中で電解クロム酸処理を行って製造
するティンフリースチールにおいて、表面の水和酸化ク
ロム膜がS10≧0.18のS7含み、210℃で12
分間空焼した後のアルカリ可溶分が30チ以上であるこ
とを特徴とする接着性のすぐれたティンフリースチール
A thin 5III plate is cathodically treated in an aqueous solution containing chromium to perform electroplating mainly consisting of metallic chromium, followed by reverse electrolytic treatment in a chromium-containing water solution using a steel plate as an anode. Consists of acids, dichromic acid and dichromic hydrochloric acid! In tin-free steel produced by electrolytic chromic acid treatment in an aqueous solution containing 1 at or more selected from IP, the hydrated chromium oxide film on the surface contains S7 with S10≧0.18 and has a
A tin-free steel with excellent adhesive properties, which has an alkali-soluble content of 30 or more after dry firing for a minute.
JP21141583A 1983-11-10 1983-11-10 Tin-free steel having excellent adhesive properties Granted JPS60103200A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21141583A JPS60103200A (en) 1983-11-10 1983-11-10 Tin-free steel having excellent adhesive properties

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21141583A JPS60103200A (en) 1983-11-10 1983-11-10 Tin-free steel having excellent adhesive properties

Publications (2)

Publication Number Publication Date
JPS60103200A true JPS60103200A (en) 1985-06-07
JPS6234838B2 JPS6234838B2 (en) 1987-07-29

Family

ID=16605573

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21141583A Granted JPS60103200A (en) 1983-11-10 1983-11-10 Tin-free steel having excellent adhesive properties

Country Status (1)

Country Link
JP (1) JPS60103200A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57177998A (en) * 1981-04-25 1982-11-01 Kawasaki Steel Corp Production of tin-free steel plate
JPS58177489A (en) * 1982-04-13 1983-10-18 Kawasaki Steel Corp Production of tin-free steel plate
JPS58177490A (en) * 1982-04-13 1983-10-18 Kawasaki Steel Corp Production of tin-free steel plate
JPS58177491A (en) * 1982-04-13 1983-10-18 Kawasaki Steel Corp Production of tin-free steel plate

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57177998A (en) * 1981-04-25 1982-11-01 Kawasaki Steel Corp Production of tin-free steel plate
JPS58177489A (en) * 1982-04-13 1983-10-18 Kawasaki Steel Corp Production of tin-free steel plate
JPS58177490A (en) * 1982-04-13 1983-10-18 Kawasaki Steel Corp Production of tin-free steel plate
JPS58177491A (en) * 1982-04-13 1983-10-18 Kawasaki Steel Corp Production of tin-free steel plate

Also Published As

Publication number Publication date
JPS6234838B2 (en) 1987-07-29

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