JPH0711070B2 - Galvanized steel sheet with excellent weldability, pressability and chemical conversion treatment - Google Patents
Galvanized steel sheet with excellent weldability, pressability and chemical conversion treatmentInfo
- Publication number
- JPH0711070B2 JPH0711070B2 JP20285090A JP20285090A JPH0711070B2 JP H0711070 B2 JPH0711070 B2 JP H0711070B2 JP 20285090 A JP20285090 A JP 20285090A JP 20285090 A JP20285090 A JP 20285090A JP H0711070 B2 JPH0711070 B2 JP H0711070B2
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- steel sheet
- oxide
- chemical conversion
- zinc
- oxide film
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Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、溶接性、プレス性、化成処理性に優れた亜鉛
系めっき鋼板に関するものである。TECHNICAL FIELD The present invention relates to a zinc-based plated steel sheet having excellent weldability, pressability and chemical conversion treatability.
(従来の技術) 亜鉛系めっき鋼板の溶接性を向上させる方法としては、
例えば特開昭55-110783号公報に示される如く、めっき
鋼板表面にAl2O3等の酸化物皮膜を生成せしめ、該酸化
物の高融点、高電気抵抗を利用し、溶接性を向上させる
とともに電極チップとめっき金属との接触を妨げ、チッ
プの溶損を防止して寿命延長を図ることが提案されてい
る。(Prior Art) As a method for improving the weldability of a zinc-based plated steel sheet,
For example, as shown in Japanese Patent Laid-Open No. 55-110783, an oxide film such as Al 2 O 3 is formed on the surface of a plated steel sheet, and the high melting point and high electric resistance of the oxide are used to improve the weldability. At the same time, it has been proposed that the contact between the electrode tip and the plated metal is prevented to prevent melting damage of the tip to extend the life.
また、特開昭59-104463号公報に示される如く、メッキ
鋼板の表面に加熱処理により、ZnO/Zn比を0.1〜0.70に
した酸化膜を生成させ、同様に溶接性を向上させること
が提案されている。Further, as disclosed in JP-A-59-104463, it is proposed to heat-treat the surface of a plated steel sheet to form an oxide film having a ZnO / Zn ratio of 0.1 to 0.70 and similarly improve weldability. Has been done.
しかしながら、このような方法においても、未だ工業的
規模では満足すべき結果が得られ難く、めっき鋼板にお
ける溶接性の向上が強く要望されている。However, even with such a method, it is still difficult to obtain satisfactory results on an industrial scale, and there is a strong demand for improvement in weldability of plated steel sheets.
また、亜鉛めっき鋼板のプレス性を向上させる方法とし
ては、例えば、特開昭62-185883号公報に記載の如く、
めっき鋼板表面に電解クロメート処理を施し、Cr2O3の
酸化物皮膜を生成せしめる方法や、特開昭62-192597号
公報に記載の如く、亜鉛系めっき鋼板上に硬い皮膜を形
成し、プレス時のめっきとダイスのかじりを防止してプ
レスの潤滑性の向上を図る方法が開示されている。As a method for improving the pressability of the galvanized steel sheet, for example, as described in JP-A-62-185883,
A method of forming an oxide film of Cr 2 O 3 by subjecting the plated steel plate surface to electrolytic chromate treatment and forming a hard film on a zinc-based plated steel plate as described in JP-A-62-192597, and pressing There is disclosed a method of improving the lubricity of a press by preventing galling and die galling at the time.
更に特開平1-136952号公報に記載の如く、めっき鋼板の
表面に有機潤滑皮膜や潤滑油等の有機物を塗布または被
覆し、プレス性を向上させることが開示されている。Further, as described in JP-A 1-136952, it is disclosed that the surface of a plated steel sheet is coated or coated with an organic material such as an organic lubricating film or a lubricating oil to improve pressability.
(発明が解決しようとする課題) しかしながら、このような製品は自動車ユーザー等の使
用において、以下のような不十分な点がある。(Problems to be Solved by the Invention) However, such products have the following inadequate points when used by automobile users and the like.
自動車ユーザーでの使用工程の概略は、鋼板を油で洗浄
する工程、プレス工程、脱脂工程、化成処理工程、塗装
工程からなっているので、電解クロメート処理鋼板の場
合は、化成処理工程で化成処理皮膜が形成せず、また潤
滑油や潤滑皮膜などを鋼板に塗布した鋼板の場合は、清
浄工程で油が落ちるので十分な潤滑性能を発揮しない。
さらには、化成処理前の脱脂工程に負荷がかかりコスト
が高くなる。一方、亜鉛系めっき鋼板に鉄−亜鉛合金フ
ラッシュめっきを施したものは電解クロメート処理に比
較して鋼板のコストが高くなる等の問題点があり、低コ
ストで、化成処理が可能で、脱脂等の工程に負荷をかけ
ず、プレス性に優れる亜鉛系めっき鋼板の開発が望まれ
ている。The outline of the process used by automobile users consists of the process of washing the steel plate with oil, the pressing process, the degreasing process, the chemical conversion treatment process, and the painting process.In the case of electrolytic chromate treated steel plates, the chemical conversion treatment is performed in the chemical conversion treatment process. In the case of a steel sheet on which no coating film is formed and a lubricating oil or a lubricating coating is applied to the steel sheet, the oil falls off in the cleaning process, so that sufficient lubricating performance is not exhibited.
Furthermore, the degreasing process before the chemical conversion treatment imposes a load, resulting in an increase in cost. On the other hand, zinc-plated steel sheets that have been subjected to iron-zinc alloy flash plating have problems such as higher steel sheet costs compared to electrolytic chromate treatment, low cost, chemical conversion treatment, degreasing, etc. It is desired to develop a zinc-based plated steel sheet that is excellent in pressability without imposing a load on the above process.
更に上記の如き、溶接性、プレス性とあいまって化成処
理性にも優れた亜鉛系めっき鋼板が強く要望されてい
る。Further, as described above, there is a strong demand for a zinc-based plated steel sheet which is excellent in chemical conversion treatment in combination with weldability and pressability.
(課題を解決するための手段) 本発明の要旨とするところは下記のとおりである。(Means for Solving the Problems) The gist of the present invention is as follows.
(1) 亜鉛系めっき鋼板表面にZnO量で30〜3000mg/m2
の酸化物、その上層にMn酸化物、P酸化物、Mo酸化物、
Co酸化物、Ni酸化物、Ca酸化物、W酸化物、V酸化物あ
るいはホウ酸の1種または2種以上を1〜500mg/m2(酸
化物中の金属量として)を被覆してなることを特徴とす
る溶接性、プレス性、化成処理性に優れた亜鉛系めっき
鋼板。(1) ZnO content on the surface of zinc-plated steel sheet is 30 to 3000 mg / m 2
Oxide, Mn oxide, P oxide, Mo oxide,
Co oxide, Ni oxide, Ca oxide, W oxide, V oxide, or one or more of boric acid is coated at 1 to 500 mg / m 2 (as the amount of metal in the oxide). A zinc-based plated steel sheet having excellent weldability, pressability, and chemical conversion treatment characteristics.
(2) 上層酸化物層中にSiO2、TiO2、Al2O3の1種また
は2種以上を1〜500mg/m2含有せしめた前項1に記載の
溶接性、プレス性、化成処理性に優れた亜鉛系めっき鋼
板。(2) The weldability, pressability, and chemical conversion treatability according to the above 1, wherein the upper oxide layer contains 1 to 500 mg / m 2 of one or more of SiO 2 , TiO 2 , and Al 2 O 3 . Excellent zinc-based plated steel sheet.
本発明の対象とする亜鉛系めっき鋼板は、溶融めっき
法、電気めっき法、蒸着めっき法、溶射法など各種の製
造方法によるものであり、めっき組成としては純Znの
他、ZnとFe,ZnとNi,ZnとAl,ZnとMn,ZnとCr,ZnとPなどZ
nを主成分として、耐食性など諸機能の向上のため1種
ないし2種以上の合金元素および不純物元素を含む。The zinc-based plated steel sheet of the present invention is a hot-dip galvanizing method, an electroplating method, a vapor deposition plating method, a thermal spraying method, and various other manufacturing methods.The plating composition is pure Zn, Zn and Fe, and Zn. And Ni, Zn and Al, Zn and Mn, Zn and Cr, Zn and P, etc. Z
Containing n as a main component and one or more alloy elements and impurity elements for improving various functions such as corrosion resistance.
また、SiO2,Al2O3などのセラミック微粒子、TiO2などの
酸化物、有機高分子をめっき層中に分散させたものがあ
り、めっき層の厚み方向で単一組成のもの、連続的ある
いは層状に組成が変化するものがある。およびこれらの
めっき上にZnを主成分とする粒子を分散させた有機皮膜
を被覆させた鋼板も対象とする。例えば、溶融亜鉛めっ
き鋼板のめっき層と素地の鉄を加熱して合金化させた合
金化溶融亜鉛めっき鋼板、電気めっき法または蒸着めっ
き法により亜鉛とその合金(例えば、鉄,ニッケル,ク
ローム等との合金)をめっきした鋼板およびこれを200
〜550℃に加熱して素地の鉄と合金化した鋼板、さらに
単一合金層のみならず、例えば電気めっき法で複層合金
めっきとしたもの、めっき層中にSiO2,Al2O3等のセラミ
ック粒子を分散させたもの、これらのめっき層の上か、
または直接鋼板上に亜鉛粒子を含む有機皮膜を被覆せし
めたものがある。防錆鋼板の形態としては、両面めっ
き、片面めっきおよび上下面に互いに異なるめっきを施
した異種めっき鋼板がある。There are also ceramic fine particles such as SiO 2 and Al 2 O 3 , oxides such as TiO 2 and organic polymers dispersed in the plating layer. Alternatively, there is a layered composition. Further, a steel sheet coated with an organic film in which particles containing Zn as a main component are dispersed is also covered. For example, an alloyed hot-dip galvanized steel sheet obtained by heating a galvanized steel sheet and a base iron to form an alloy, zinc and its alloys (for example, iron, nickel, chrome, etc. by electroplating or vapor deposition plating). Alloy) and a steel plate
Steel sheet alloyed with base iron by heating to ~ 550 ° C, not only single alloy layer but also multi-layer alloy plating by electroplating method, SiO 2 , Al 2 O 3 etc. in the plating layer Dispersed ceramic particles, on these plated layers,
Alternatively, there is a steel sheet directly coated with an organic coating containing zinc particles. As the form of the rustproof steel plate, there are a double-sided plating, a single-sided plating, and a dissimilar plated steel plate having different platings on the upper and lower surfaces.
本発明者らは、亜鉛めっき鋼板の種類の如何によらず、
めっきがZnを主成分とする限り、めっき鋼板の表面にZn
Oを形成させることにより、スポット溶接において電極
チップ先端にFe,Znを主成分とする電極保護金属を生成
させ、以って電極チップ寿命を大幅に改善することを見
出した。The present inventors, regardless of the type of galvanized steel sheet,
As long as the plating is mainly composed of Zn, the surface of the plated steel is Zn
It was found that by forming O, electrode protection metal containing Fe and Zn as the main components is generated at the tip of the electrode tip in spot welding, and the life of the electrode tip is greatly improved.
従来の上記めっき鋼板においては、ZnOを主体とする酸
化膜を溶接性によいとされるZnO量で30〜3000mg/m2(片
面当たり)生成させることが不安定であった。ここで、
ZnOを主体とする酸化膜とは酸化物中にZnOの他、例え
ば、めっき層中に含有する成分元素またはそれらの酸化
物などの化合物等を含有するものでもよい。また、陽極
酸化などの電気化学処理において、処理液が含有する成
分あるいは化合物を含んでもよい。In the above-mentioned conventional plated steel sheet, it was unstable to form an oxide film mainly composed of ZnO in an amount of ZnO of 30 to 3000 mg / m 2 (per surface) which is considered to have good weldability. here,
The oxide film mainly composed of ZnO may be, for example, a film containing not only ZnO in the oxide but also a component element contained in the plating layer or a compound such as an oxide thereof. In addition, in an electrochemical treatment such as anodization, a component or compound contained in the treatment liquid may be contained.
本発明者らは亜鉛めっき層表面に、ZnOを主体とする酸
化膜を生成せしめるために、第1の方法として鋼板を酸
含有の酸化剤水溶液に接触させることで、ZnOを主体す
る酸化膜をZnO量で30〜3000mg/m2(片面当たり)生成さ
せることが容易になり、溶接性に優れた亜鉛系めっき鋼
板を提供し得ることを見出した。酸の働きは、めっき層
表面をいくらか溶解してめっき層からZn等のイオンを供
給し、かつめっき層に接触する溶液中のpHを高くするこ
とであり、酸化剤はそのめっき層表面にて浴中のZn等を
酸化してめっき層表面にZnOを主体とする酸化膜を形成
する働きをする。In order to form an oxide film mainly composed of ZnO on the surface of the galvanized layer, the present inventors contact the steel sheet with an acid-containing oxidant aqueous solution as a first method to form an oxide film mainly composed of ZnO. It has been found that it becomes easy to generate 30 to 3000 mg / m 2 (per one side) with a ZnO amount, and a zinc-based plated steel sheet having excellent weldability can be provided. The function of the acid is to dissolve some of the plating layer surface to supply ions such as Zn from the plating layer, and to increase the pH of the solution in contact with the plating layer, and the oxidizer at the plating layer surface. It functions to oxidize Zn etc. in the bath to form an oxide film mainly composed of ZnO on the surface of the plating layer.
酸化剤として、例えばHNO310〜100g/lを含有すること
で、Zn等を酸化してめっき層表面にZnOを主体とする酸
化膜を形成することができる。HNO3の下限を10g/lとし
たのはそれ未満では酸化がしにくくなり、酸化膜を生成
することができなくなるためである。また、HNO3の上限
を100g/lとしたのはそれを超えて含有しても酸化剤とし
ての効果が飽和し、合金層表面のZnとFeを溶解し、特に
Feを溶解することで、Feの酸化物の生成が多くなり、ス
ポット溶接チップ寿命の改善の効果が低くなるためであ
る。By containing, for example, 10 to 100 g / l of HNO 3 as an oxidizing agent, Zn or the like can be oxidized to form an oxide film mainly containing ZnO on the surface of the plating layer. The lower limit of HNO 3 is set to 10 g / l because if it is less than that, it becomes difficult to oxidize and an oxide film cannot be formed. Further, the upper limit of HNO 3 is set to 100 g / l, the effect as an oxidant is saturated even if it is contained in excess of that, dissolves Zn and Fe on the surface of the alloy layer,
This is because the dissolution of Fe increases the amount of Fe oxide produced and reduces the effect of improving the life of the spot welding tip.
さらに酸化剤として、KMnO4,Ca(ClO)2,K2Cr2O7,NaClO3,
ClO2,KNO3,NaNO3等を添加することにより、表面皮膜の
生成が促進される。Furthermore, as an oxidizing agent, KMnO 4 , Ca (ClO) 2 , K 2 Cr 2 O 7 , NaClO 3 ,
By adding ClO 2 , KNO 3 , NaNO 3, etc., the formation of the surface film is promoted.
鋼板にZn(NO3)2とHNO3の水溶液を接触させる方法として
は浸漬、スプレーによる噴射等いずれの方法でもよい。
また、浸漬、スプレーによる噴射後、例えば表面に乾燥
加熱ガスを吹きつけたり、鋼板を約100℃以下に加熱す
れば、より薄い溶液でも水分の蒸発により濃縮液とな
り、かつ高温で反応するので効果的に処理することがで
きる。As a method for bringing the aqueous solution of Zn (NO 3 ) 2 and HNO 3 into contact with the steel sheet, any method such as dipping or spraying may be used.
Also, after spraying by dipping or spraying, for example, if a dry heating gas is blown to the surface or the steel sheet is heated to about 100 ° C or less, even a thinner solution becomes a concentrated solution due to evaporation of water and reacts at high temperature, which is effective. Can be processed.
かくして、酸化膜生成処理を行うことで生成した酸化膜
等の組成はZnOを主体としてFeの酸化物、ZnおよびFeの
水酸化物で、これらは単体でも混合していても、Al等の
不純物を含んでいてもかまわない。しかし、表面皮膜と
しての特性からは、表面を均一に覆い、皮膜抵抗が低く
なるZnO成分の多い酸化膜が望ましい。Thus, the composition of the oxide film and the like generated by performing the oxide film generation treatment is ZnO as a main component of Fe oxide, Zn and Fe hydroxide, which may be a single substance or a mixture of impurities such as Al. May be included. However, an oxide film containing a large amount of ZnO component, which uniformly covers the surface and has a low film resistance, is desirable from the characteristics of the surface film.
ZnOを主体とする酸化膜を生成せしめるために、Znイオ
ンの補給剤としてZn(NO3)2100〜600g/lとすることで、
酸化剤水溶液のpHが4以下であればめっき層表面の活性
化に寄与し、ZnOを生成せしめるためのZnイオンの供給
ができる。In order to form an oxide film mainly composed of ZnO, by using Zn (NO 3 ) 2 100 to 600 g / l as a supplementary agent for Zn ions,
When the pH of the oxidant aqueous solution is 4 or less, it contributes to activation of the surface of the plating layer, and Zn ions can be supplied to generate ZnO.
Zn(NO3)2の下限を100g/lとしたのはそれ未満では合金層
表面のZnイオンとして不十分で酸化膜を生成することが
できなくなるためである。また、その上限を600g/lとし
たのはそれを超えると皮膜が多く生成しすぎて、抵抗が
大きくなり、溶接時の電極チップとの抵抗発熱により、
電極チップ径の拡大による溶接性劣化の原因になるから
である。The lower limit of Zn (NO 3 ) 2 is set to 100 g / l because if it is less than that, Zn oxide on the surface of the alloy layer is insufficient and an oxide film cannot be generated. In addition, the upper limit of 600 g / l is that if it exceeds that, too much film will be generated, resistance will become large, and due to resistance heat generation with the electrode tip during welding,
This is because the increase in electrode tip diameter causes deterioration of weldability.
処理浴にはめっき中のFeやZn、不純物としてのMn,Al,P,
Si等が溶け出すことがある。これらの中でZnイオンをあ
らかじめ浴中に添加しておくとZnイオンをめっき層中か
ら溶かして供給する必要がなくなり、より短時間でZnO
の析出が起こるので好ましい。なお、他の不純物の溶出
はできるだけ少量に抑制することが望ましい。特に、Fe
は1g/lを超えて含有すると表面にFeの酸化物、水酸化物
が生成して表面が黄変し、鋼板表面の商品品位を悪化さ
せるとともに、Feの酸化物、水酸化物が抵抗皮膜とな
り、スポット溶接チップ寿命が低下する。従って、本発
明ではFeイオン濃度を規定するものではないが、できる
だけ低くすることが望ましい。The treatment bath contains Fe and Zn in the plating, Mn, Al, P as impurities,
Si etc. may melt out. Of these, if Zn ions are added to the bath beforehand, it is not necessary to dissolve and supply Zn ions from the plating layer, and ZnO can be used in a shorter time.
Is preferable because it causes precipitation of. In addition, it is desirable to suppress elution of other impurities to be as small as possible. Especially Fe
When it contains more than 1 g / l, Fe oxides and hydroxides are generated on the surface and the surface turns yellow, deteriorating the product quality of the steel sheet surface, and Fe oxides and hydroxides are resistance films. Therefore, the life of the spot welding tip is shortened. Therefore, the Fe ion concentration is not specified in the present invention, but it is desirable to make it as low as possible.
ZnOを主体とする酸化膜を生成せしめるために、鋼板をZ
n(NO3)2100〜600g/lとHNO310〜100g/lを含有する酸化剤
水溶液に浴温30〜80℃で、0.2〜10秒間接触をさせるこ
とにより、酸化膜生成処理を行うことができる。In order to form an oxide film mainly composed of ZnO, the steel plate is Z
N (NO 3 ) 2 100-600 g / l and HNO 3 10-100 g / l are added to the oxidant aqueous solution at a bath temperature of 30-80 ° C for 0.2-10 seconds to form an oxide film. be able to.
処理浴温を30〜80℃とし、下限を30℃としたのは、めっ
き表面のZnイオンの酸化を容易にするためであり、それ
未満では反応速度が遅く、表面皮膜を得にくいためであ
る。また、上限を80℃としたのは、反応が進行しすぎ
て、過度に酸化皮膜が発生し、溶接性を悪くするためで
ある。もっとも、温度が80℃を超えても接触時間を短く
すればよいが、時間を短くしたときの温度を高温に制御
することが困難なため、温度は80℃以下とするのが望ま
しい。The treatment bath temperature was set to 30 to 80 ° C and the lower limit was set to 30 ° C to facilitate the oxidation of Zn ions on the plating surface, and below that, the reaction rate was slow and it was difficult to obtain a surface film. . Further, the upper limit is set to 80 ° C. because the reaction proceeds too much and an oxide film is excessively generated to deteriorate the weldability. Of course, the contact time may be shortened even if the temperature exceeds 80 ° C, but it is difficult to control the temperature at a high temperature when the time is shortened, so the temperature is preferably 80 ° C or lower.
そのために、ライン速度との兼ね合いにもよるが、浸漬
またはスプレー等の接触処理時間を0.2〜10秒としたの
は、0.2秒未満では酸化膜生成処理が不十分で、溶接性
が向上しないためであり、10秒を超えて処理しても酸化
膜の生成は多くなりすぎて、溶接性を悪くするためであ
る。Therefore, depending on the balance with the line speed, the contact treatment time such as dipping or spraying was set to 0.2 to 10 seconds because the oxide film generation treatment is insufficient if it is less than 0.2 seconds and the weldability does not improve. The reason is that even if the treatment is performed for more than 10 seconds, the oxide film is excessively generated and the weldability is deteriorated.
また、第2の方法としては、例えば、Zn(NO3)2・6H2O:40
0g/l、HNO3:1g/lの水溶液中で、亜鉛系めっき鋼板を陰
極として、電流密度1〜20A/dm2、処理時間0.5〜10秒で
溶接性に優れた酸化物を生成せしめることができる。As the second method, for example, Zn (NO 3 ) 2 .6H 2 O: 40
In an aqueous solution of 0 g / l, HNO 3 : 1 g / l, using zinc-based plated steel sheet as a cathode, current density of 1 to 20 A / dm 2 and treatment time of 0.5 to 10 seconds to generate an oxide with excellent weldability. You can
更に第3の方法としては、溶融めっき、電気めっき或い
は蒸着めっき後、合金化処理、酸化膜生成処理を行うこ
とで、ZnOを主体とする酸化膜を確実に生成することが
できる。その具体的な方法としては、例えば合金化溶融
亜鉛めっき鋼板を製造する合金化炉を、板温が400〜800
℃になるように調整し、該炉中を表面まで合金化が完了
する速度で通過させ、続いて雰囲気の露点を確保するた
めに気水ノズルで水と空気を噴射する気水処理すること
で効果的に酸化膜生成反応を行わせることもできる。さ
らに、ライン外で溶融めっき、電気めっきあるいは蒸着
めっき後、合金化処理、酸化膜生成処理を行うことで、
ZnOを主体とする酸化膜を確実に生成させることができ
る。その方法も、前記の方法に類似の方法を採れば、Zn
Oを主体とする酸化膜生成反応を確実にかつ効果的に行
うことができる。Furthermore, as a third method, an oxide film mainly composed of ZnO can be reliably produced by performing an alloying treatment and an oxide film producing treatment after hot dipping, electroplating or vapor deposition plating. As a specific method, for example, an alloying furnace for producing an alloyed hot-dip galvanized steel sheet, the plate temperature is 400 ~ 800
By adjusting the temperature to reach 0 ° C., passing through the furnace to the surface at a speed at which alloying is completed, and then performing steam treatment by spraying water and air with a steam nozzle to secure the dew point of the atmosphere. It is also possible to effectively carry out the oxide film formation reaction. Furthermore, after hot-dip plating, electroplating or vapor deposition plating outside the line, alloying treatment and oxide film generation treatment are performed.
An oxide film mainly composed of ZnO can be reliably generated. As for the method, if a method similar to the above method is adopted, Zn
Oxide-based oxide film formation reaction can be reliably and effectively performed.
なお、酸化膜生成処理は上記の気水処理の他に、蒸気を
めっき表面に噴射してZnOを主体とする酸化膜を生成さ
せたり、ライン外で、露点を酸化雰囲気に調整した加熱
炉で熱処理を行ってZnOを主体とする酸化膜を生成させ
る等、いずれの方法を採ってもよい。In addition to the above steam-water treatment, the oxide film generation treatment may be performed by injecting steam onto the plating surface to generate an oxide film mainly composed of ZnO, or outside the line in a heating furnace whose dew point is adjusted to an oxidizing atmosphere. Any method such as heat treatment to form an oxide film mainly composed of ZnO may be adopted.
このようにして亜鉛系めっき鋼板の表面に溶接性に優れ
た酸化物としてZnO主体酸化物を30〜3000mg/m2生成せし
め、その上層に下記の如くプレス性、化成処理性に優れ
た酸化物を生成せしめることができる。In this way, ZnO-based oxides of 30 to 3000 mg / m 2 were produced as oxides with excellent weldability on the surface of the zinc-based plated steel sheet, and oxides excellent in pressability and chemical conversion treatment were formed on the upper layer as follows. Can be generated.
プレスの潤滑性を付与するには、表面に硬質の皮膜を形
成することが有効である。この点で電解クロメート処
理、鉄亜鉛合金めっきは有効であるが、前者は化成処理
皮膜が形成できず、後者は処理量が多くコスト高にな
る。In order to impart the lubricity of the press, it is effective to form a hard film on the surface. In this respect, electrolytic chromate treatment and iron-zinc alloy plating are effective, but the former cannot form a chemical conversion treatment film, and the latter requires a large amount of treatment, resulting in high cost.
これらの問題を解決し得るめっき鋼板表面の硬質皮膜と
しては、酸化物皮膜であって、かつ化成処理液中で溶解
し、化成皮膜を形成できるとともに、皮膜成分が化成処
理液に溶け出しても化成処理に悪影響を与えないことが
必要である。The hard coating on the surface of the plated steel sheet that can solve these problems is an oxide coating and can be dissolved in a chemical conversion treatment liquid to form a chemical conversion coating, and even if the coating components are dissolved in the chemical conversion treatment liquid. It is necessary not to adversely affect the chemical conversion treatment.
本発明者等は、このような観点から、表面にMn,P,Mo,C
o,Ni,Ca,W,V,Bの1種または2種以上からなる酸化物系
皮膜を形成すれば良いことを見出した。この酸化物皮膜
はクロメート皮膜と同様ガラス状の皮膜となり、プレス
時にめっきのダイスへのかじりを抑制し、摺動性を良好
とする。さらに、化成処理液には溶解するため、クロメ
ート皮膜と異なり、化成処理皮膜を形成することがで
き、また化成処理皮膜の成分でもあるため、化成処理液
に溶け出しても悪影響はない。The inventors of the present invention, from such a viewpoint, Mn, P, Mo, C on the surface.
It has been found that it is sufficient to form an oxide film composed of one or more of o, Ni, Ca, W, V and B. This oxide film becomes a glass-like film like the chromate film, and suppresses galling of the plating die during pressing and improves slidability. Furthermore, since it dissolves in the chemical conversion treatment liquid, unlike the chromate film, a chemical conversion treatment film can be formed, and since it is also a component of the chemical conversion treatment film, there is no adverse effect even if it dissolves into the chemical conversion treatment liquid.
酸化物皮膜の構造は明確ではないが、Mn−O結合、その
他金属−O結合、P−O結合、B−O結合、Si−O結
合、Ti−O結合、Al−O結合からなるネットワークが主
体で、部分的に−OH、CO3基等が、さらにはめっきから
供給される金属が置換したアモルファス状の巨大分子構
造であろうと推定している。Although the structure of the oxide film is not clear, a network consisting of Mn-O bond, other metal-O bond, P-O bond, B-O bond, Si-O bond, Ti-O bond, Al-O bond is formed. It is presumed that the main component is an amorphous macromolecular structure in which —OH, CO 3 groups, etc. are partially replaced by the metal supplied from the plating.
また、この皮膜は酸化膜皮膜のため、油による洗浄工程
や、脱油工程でも溶解しないので、潤滑性能の低下や、
他の工程に負荷を与えない。In addition, since this film is an oxide film, it does not dissolve even in the oil cleaning process and the oil removal process, so the lubrication performance is reduced,
Does not impose a load on other processes.
酸化物皮膜の密着性、成膜性を向上させるためにリン酸
又はホウ酸とコロイダルSiO2、コロイダルTiO2、コロイ
ダルAl2O3の1種又は2種以上500mg/m2以下(P,SiO2,Ti
O2,Al2O3として)を混入する。かくして、酸化物の皮膜
構造が均一化し、成膜性も向上し、プレス成形性が良好
になり、又化成処理性をも向上することができる。Phosphoric acid or boric acid and colloidal SiO 2 , colloidal TiO 2 , or colloidal Al 2 O 3 in order to improve the adhesion and film-forming property of the oxide film. One or more of them and 500 mg / m 2 or less (P, SiO 2 2 , Ti
O 2 and Al 2 O 3 ) are mixed. Thus, the oxide film structure can be made uniform, the film forming property can be improved, the press moldability can be improved, and the chemical conversion treatment property can also be improved.
このような酸化物皮膜は、亜鉛系めっき鋼板を水溶液中
へ浸漬するか、水溶液を散布するか、又は水溶液中で陰
極電解処理することにより確実に生成させることができ
る。このときに前記の如きめっき金属の亜鉛、亜鉛合金
めっきの場合は、亜鉛と合金元素(金属)、水溶液中の
不純物等がその他の酸化物として混入する。Such an oxide film can be reliably produced by immersing a zinc-based plated steel sheet in an aqueous solution, spraying the aqueous solution, or subjecting the zinc-based plated steel sheet to a cathodic electrolysis treatment in the aqueous solution. At this time, in the case of zinc or zinc alloy plating of the plating metal as described above, zinc, alloy elements (metals), impurities in the aqueous solution and the like are mixed as other oxides.
次に、本発明の皮膜の皮膜量範囲について述べる。Next, the coating amount range of the coating of the present invention will be described.
酸化物の皮膜量はプレス性を良好とするには、金属とし
て1mg/m2以上あればよいが、皮膜量が500mg/m2を越える
と化成処理皮膜の形成が不十分となる。ゆえに、酸化物
の適正な皮膜量は、金属として1〜500mg/m2、好ましく
は1〜200mg/m2である。The amount of oxide film should be 1 mg / m 2 or more as a metal in order to improve pressability, but if the amount of film exceeds 500 mg / m 2 , formation of the chemical conversion treatment film becomes insufficient. Therefore, the proper coating weight of oxides, 1-500 mg / m 2 as metal, and preferably 1 to 200 mg / m 2.
次にコロイダルSiO2、コロイダルTiO2、コロイダルAl2O
3の1種又は2種以上の合計量としては500mg/m2以下(S
iO2、TiO2、Al2O3として)、好ましくは200mg/m2以下がよ
く、500mg/m2超になると化成処理性が劣化することがあ
る。下限は1mg/m2で十分である。Next, colloidal SiO 2 , colloidal TiO 2 , colloidal Al 2 O
The total amount of one or more of 3 is 500 mg / m 2 or less (S
iO 2 , TiO 2 , and Al 2 O 3 ), preferably 200 mg / m 2 or less, and if it exceeds 500 mg / m 2 , chemical conversion treatability may deteriorate. A lower limit of 1 mg / m 2 is sufficient.
次に上記のごとき酸化物皮膜の生成方法としては、例え
ばMn系酸化物としては、過マンガン酸カリウム、リン
酸、ホウ酸、ホウ酸ナトリウム、モリブデン酸アンモニ
ウム、リンモリブデン酸、タングステン酸アンモニウ
ム、リンタングステン酸、ケイタングステン酸、バナジ
ン酸アンモニウム、コバルト、ニッケル、カルシウム等
の塩化物、硫酸塩、あるいはリン酸塩として1g/l〜溶解
限、反応を促進するためリン酸、硫酸、硝酸、塩酸等添
加した浴を用いる。Next, as a method for forming the oxide film as described above, for example, as the Mn-based oxide, potassium permanganate, phosphoric acid, boric acid, sodium borate, ammonium molybdate, phosphomolybdic acid, ammonium tungstate, phosphorus, etc. Tungstic acid, silicotungstic acid, ammonium vanadate, chlorides such as cobalt, nickel, and calcium, sulfates, or phosphates from 1 g / l to the solubility limit, phosphoric acid, sulfuric acid, nitric acid, hydrochloric acid, etc. to accelerate the reaction. Use the added bath.
SiO2、TiO2、Al2O3としては、それぞれコロイド微粒子水
溶液、ケイフッ化カリウム、チタンフッ化カリウム等を
固体として1〜60g/l添加することができる。As SiO 2 , TiO 2 , and Al 2 O 3 , 1 to 60 g / l of an aqueous colloidal fine particle solution, potassium silicofluoride, potassium titanium fluoride or the like can be added as a solid.
このような水溶液に前記のごとき亜鉛系めっき鋼板を浸
漬するか、水溶液を散布するか、又は水溶液中で電解処
理することにより確実に皮膜を生成することができる。The zinc-based plated steel sheet as described above may be dipped in such an aqueous solution, the aqueous solution may be sprayed, or an electrolytic treatment may be performed in the aqueous solution to form a film reliably.
このようにして酸化物皮膜が生成すると、めっき層及び
めっき層中の合金金属の一部が酸化物皮膜中へ、その他
酸化物として混入する。When the oxide film is formed in this manner, part of the plating layer and the alloy metal in the plating layer is mixed into the oxide film as other oxide.
(実施例) 次に本発明の実施例を比較例と共に、下記の表に示す。(Examples) Next, examples of the present invention are shown in the following table together with comparative examples.
注1) めっき鋼板の種類:AS:合金化溶融亜鉛めっき鋼
板(Fe10%,Al10.25%,残Zn),EG:電気亜鉛めっき鋼
板,GI:溶融亜鉛めっき鋼板(Al0.3%,Fe0.8%,Pb0.1
%,残Zn),HA:半合金化溶融亜鉛めっき鋼板(Fe5%,Al
0.3%,残Zn),鋼板厚はいずれも0.8mmの普通鋼,Zn/Zn
-Cr:12%Cr含有電気合金めっき上層に電気亜鉛めっき1g
/m2鋼板 注2) ZnO皮膜処理条件 ・ 浸漬:Zn(NO3)2・6H2O:400g/l、HNO3:70g/lの50℃水
溶液中に1〜10秒間亜鉛系めっき鋼板を浸漬してZnO皮
膜を生成せしめた。 Note 1) Type of galvanized steel sheet: AS: hot-dip galvanized steel sheet (Fe10%, Al10.25%, residual Zn), EG: galvanized steel sheet, GI: hot-dip galvanized steel sheet (Al0.3%, Fe0. 8%, Pb0.1
%, Residual Zn), HA: Semi-alloyed galvanized steel sheet (Fe5%, Al
0.3%, residual Zn), normal steel with a steel plate thickness of 0.8 mm, Zn / Zn
-Cr: 1% electrogalvanized on top of electroalloy plating containing 12% Cr
/ m 2 Steel plate Note 2) ZnO coating treatment conditions ・ Immersion: Zn (NO 3 ) 2・ 6H 2 O: 400g / l, HNO 3 : 70g / l 50 ° C aqueous solution for 1 to 10 seconds It was dipped to form a ZnO film.
・ 電解:Zn(NO3)2・6H2O:400g/l、HNO3:1g/l水溶液中
で亜鉛系めっき鋼板を陰極として電流密度7A/dm2、1〜
7秒電解によりZnO皮膜を生成せしめた。・ Electrolysis: Zn (NO 3 ) 2・ 6H 2 O: 400 g / l, HNO 3 : 1 g / l Current density 7 A / dm 2 , 1 ~ 1 g / l aqueous solution with zinc-based plated steel plate as cathode
A ZnO film was formed by electrolysis for 7 seconds.
・ 気水噴霧:合金化処理後の亜鉛系めっき鋼板(500
℃)表面に80〜125l/分の霧化水を噴射してZnO皮膜を生
成した。・ Air / water spray: Zinc-based plated steel sheet after alloying (500
The surface was sprayed with 80-125 l / min of atomized water to form a ZnO film.
注3) 上層酸化膜生成条件 ・ Mn酸化物生成は過マンガン酸カリウム:50g/l、リン
酸10g/l、硫酸3g/l、炭酸亜鉛:5g/lの溶液(30℃)に被
処理鋼板を浸漬するかまたは該鋼板を陰極とし、Pt電極
を陽極として7A/dm2で1.5秒電解を行った後、水洗、乾
燥した。Note 3) Conditions for forming the upper oxide film ・ Mn oxide is produced by using a solution of potassium permanganate (50 g / l), phosphoric acid (10 g / l), sulfuric acid (3 g / l) and zinc carbonate (5 g / l) at 30 ° C. Or was electrolyzed at 7 A / dm 2 for 1.5 seconds using the steel plate as a cathode and the Pt electrode as an anode, followed by washing with water and drying.
・ P酸化物生成は、リン酸カリウム50g/l、リン酸10g
/lの水溶液中に亜鉛系めっき鋼板を浸漬するかまたは該
鋼板を陰極または陽極として、電解処理(5〜10A/d
m2、1〜1.5秒)した。・ P oxide production is potassium phosphate 50g / l, phosphoric acid 10g
The zinc-plated steel sheet is immersed in an aqueous solution of 1 / l or the steel sheet is used as a cathode or an anode to perform electrolytic treatment (5 to 10 A / d
m 2 , 1-1.5 seconds).
・ Mo酸化物生成はモリブデン酸アンモニウム:50g/l、
リン酸:10g/lの溶液(30℃)に被処理鋼板を浸漬するか
または該鋼板を陰極、Pt電極を陽極にして7A/dm2で1.5
秒電解を行った後、水洗、乾燥した。モリブデン酸アン
モニウム、リン酸の濃度、さらには一部には硫酸、炭酸
亜鉛の添加を行い、溶液の温度、浸漬時間、電解量を調
整して作成した。・ Mo oxide formation is ammonium molybdate: 50 g / l,
Phosphoric acid: Immerse the steel sheet to be treated in a solution of 10 g / l (30 ° C), or use the steel sheet as a cathode and the Pt electrode as an anode at 7 A / dm 2 and 1.5
After second electrolysis, it was washed with water and dried. It was prepared by adding ammonium molybdate and phosphoric acid concentrations, and partly by adding sulfuric acid and zinc carbonate, and adjusting the temperature of the solution, the immersion time, and the amount of electrolysis.
・ Co酸化物生成は硝酸コバルト:200g/l、硝酸亜鉛:15
0g/l、濃硝酸:1cc/lの溶液30℃で被処理鋼板を陰極とし
て、Pt電極と陽極にし、7A/dm2で1.5秒電解を行った
後、水洗、乾燥した。硝酸コバルト、硝酸亜鉛、硝酸の
濃度を調節し、さらには一部にはリン酸、硫酸、炭酸亜
鉛の添加を行い、溶液の温度、電解量を調整して作成し
た。・ Co oxide production is cobalt nitrate: 200 g / l, zinc nitrate: 15
A solution of 0 g / l and concentrated nitric acid: 1 cc / l At 30 ° C., the steel sheet to be treated was used as a cathode, a Pt electrode and an anode were electrolyzed at 7 A / dm 2 for 1.5 seconds, then washed with water and dried. It was prepared by adjusting the concentrations of cobalt nitrate, zinc nitrate and nitric acid, and further adding phosphoric acid, sulfuric acid and zinc carbonate to a part of them to adjust the temperature of the solution and the amount of electrolysis.
・ Ni酸化物生成は硝酸ニッケル:250g/l、硝酸亜鉛:15
0g/l、濃硝酸1cc/lの溶液30℃で被処理鋼板を陰極とし
て、Pt電極を陽極にし、7A/dm2で1.5秒電解を行った
後、水洗、乾燥した。硝酸ニッケル、硝酸亜鉛、硝酸の
濃度を調節し、さらには一部にはリン酸、硫酸、炭酸亜
鉛の添加を行い、溶液の温度、電解量を調整して作成し
た。・ Ni oxide formation is nickel nitrate: 250 g / l, zinc nitrate: 15
A solution of 0 g / l and 1 cc / l of concentrated nitric acid was used as a cathode for the steel sheet to be treated and a Pt electrode as an anode at 30 ° C., and electrolysis was performed at 7 A / dm 2 for 1.5 seconds, followed by washing with water and drying. It was prepared by adjusting the concentrations of nickel nitrate, zinc nitrate and nitric acid, and further adding phosphoric acid, sulfuric acid and zinc carbonate to a part thereof to adjust the temperature of the solution and the amount of electrolysis.
・ Ca酸化物生成は硝酸カルシウム:250g/l、濃硝酸:1c
c/lの溶液30℃で被処理鋼板を陰極として、Pt電極を陽
極にし、7A/dm2で1.5秒電解を行った後、水洗、乾燥し
た。硝酸カルシウム、硝酸の濃度を調節し、さらには一
部にはリン酸、硫酸、炭酸亜鉛の添加を行い、溶液の温
度、電解量を調整して作成した。・ Ca oxide production is calcium nitrate: 250 g / l, concentrated nitric acid: 1 c
The c / l solution was used as a cathode with the treated steel plate as a cathode and a Pt electrode as an anode at 30 ° C., and electrolysis was performed at 7 A / dm 2 for 1.5 seconds, followed by washing with water and drying. It was prepared by adjusting the concentrations of calcium nitrate and nitric acid, and further adding phosphoric acid, sulfuric acid, and zinc carbonate to some of them to adjust the temperature of the solution and the amount of electrolysis.
・ W酸化物生成はタングステン酸アンモニウム:20g/
l、リン酸:10g/lの溶液(30℃)に被処理鋼板を浸漬す
るかまたは該鋼板を陰極として、Pt電極を陽極にし、7A
/dm2で1.5秒電解を行った後、水洗、乾燥した。タング
ステン酸アンモニウム、リン酸の濃度を調節し、さらに
は一部には硫酸、炭酸亜鉛の添加を行い、溶液の温度、
浸漬時間、電解量を調整して作成した。・ W oxide production is ammonium tungstate: 20g /
l, phosphoric acid: dip the steel sheet to be treated in a solution of 10 g / l (30 ° C.) or use the steel sheet as a cathode and the Pt electrode as an anode,
After electrolysis at / dm 2 for 1.5 seconds, it was washed with water and dried. Adjust the concentrations of ammonium tungstate and phosphoric acid, and add sulfuric acid and zinc carbonate to some of them to adjust the temperature of the solution,
It was prepared by adjusting the immersion time and the amount of electrolysis.
・ V酸化物生成はバナジン酸アンモニウム:30g/l、り
ん酸:10g/lの水溶液(30℃)中で被処理鋼板を陰極とし
て、Pt電極を陽極にし、7A/dm2で1.5秒電解を行った
後、水洗、乾燥した。バナジン酸アンモニウム、リン酸
の濃度、さらには一部には硫酸、炭酸亜鉛の添加を行
い、溶液の温度、電解時間、電解量を調整して作成し
た。・ V oxide is generated by ammonium vanadate: 30 g / l, phosphoric acid: 10 g / l in an aqueous solution (30 ° C), using the steel sheet to be treated as the cathode, the Pt electrode as the anode, and electrolysis at 7 A / dm 2 for 1.5 seconds. After that, it was washed with water and dried. The concentration of ammonium vanadate and phosphoric acid, and further sulfuric acid and zinc carbonate were partially added to adjust the temperature of the solution, the electrolysis time, and the electrolysis amount.
・ ホウ素酸化物生成はホウ酸:50g/lからなる水溶液中
で、亜鉛系めっき鋼板を陰極として7A/dm2、1.5〜7秒
の電解条件で電解した。混合酸化物皮膜の生成において
は、上記それぞれの金属塩あるいは酸を添加混合した浴
を作成して行った。Boron oxide was produced by electrolysis in an aqueous solution of boric acid: 50 g / l under the electrolytic condition of 7 A / dm 2 for 1.5 to 7 seconds, using a zinc-based plated steel sheet as a cathode. The formation of the mixed oxide film was performed by preparing a bath in which the above metal salts or acids were added and mixed.
皮膜量は何れも測定元素量 注4) 化成処理性試験条件 化成処理液(亜鉛−リン酸−弗素系処理浴)にはSD5000
(日本ペイント社製)を用い、処方どおり脱脂、表面調
整を行った後化成処理を行った。化成処理皮膜の判定
は、SEM(2次電子線像)により、均一に皮膜が形成さ
れているものは○、部分的に皮膜形成されているものは
△、皮膜が形成されていないものは×と判定した。All coating amounts are measured element amounts Note 4) Chemical conversion treatment test conditions SD5000 is used for the chemical conversion treatment liquid (zinc-phosphoric acid-fluorine treatment bath).
(Manufactured by Nippon Paint Co., Ltd.), degreasing and surface preparation were performed as prescribed, and post-chemical conversion treatment was performed. The chemical conversion coating is judged by SEM (secondary electron beam image): ○ if the coating is uniformly formed, △ if it is partially coated, × if it is not coated. It was determined.
注5) プレス性試験条件および評価方法: サンプルサイズ:17mm×300mm,引張り速度:500mm/min,角
ビート肩R:1.0/3.0mm,摺動長:200mm,塗油:ノックスラ
スト530F(パーカー興産株式会社)40.1mg/m2の条件
で、面圧を100〜600kgfの間で数点試験を行い、引き抜
き加重を測定し、面圧と引き抜き加重の傾きから摩擦係
数を求めた。Note 5) Pressability test conditions and evaluation method: Sample size: 17 mm × 300 mm, pulling speed: 500 mm / min, square beat shoulder R: 1.0 / 3.0 mm, sliding length: 200 mm, oil: Knoxlast 530F (Parker Kosan) Co., Ltd.) under the condition of 40.1 mg / m 2 , the surface pressure was tested at several points between 100 and 600 kgf, the pulling load was measured, and the friction coefficient was determined from the slope of the surface pressure and the pulling load.
注6: 溶接性 溶接条件は下記による。Note 6: Weldability Welding conditions are as follows.
1) 加圧力:250kgf 2) 初期加圧時間:49Hr 3) 通電時間:12Hr 4) 保持時間:5Hr 5) 溶接電流:11KA 6) チップ先端径:5.0φ(円錐台頭型) 7) 電極寿命終点判定:溶接電流の85%でのナゲット
径が3.6mmを確保できる打点数 8) 電極材質:Cu-Cr(一般に用いられているもの) 溶接は、めっき鋼板の片面を上、他面を下として、2枚
重ね合わせて連続打点数をとった。1) Pressurizing force: 250kgf 2) Initial pressurizing time: 49Hr 3) Energizing time: 12Hr 4) Holding time: 5Hr 5) Welding current: 11KA 6) Tip tip diameter: 5.0φ (Frustum-cone type) 7) Electrode life end Judgment: Number of dots that can secure a nugget diameter of 3.6 mm at 85% of welding current 8) Electrode material: Cu-Cr (generally used) Welding is performed with one side of the plated steel sheet facing up and the other side facing down. Two sheets were piled up and the number of consecutive points was taken.
注7): ZnO皮膜の測定 5%沃素メチルアルコール溶液で、めっき層のみ溶解
し、抽出残渣で混合融剤(硼酸1,炭酸ナトリウム3)で
融解した後、塩酸で溶液化してICPで分析した亜鉛量をZ
nO量に換算。Note 7): ZnO film measurement 5% iodine methyl alcohol solution was used to dissolve only the plating layer, and the extraction residue was melted with a mixed flux (boric acid 1, sodium carbonate 3), then dissolved in hydrochloric acid and analyzed by ICP. Zinc amount to Z
Converted to nO amount.
(発明の効果) かくすることにより、スポット溶接において、連続打点
数を増加し、それだけチップを取り替えることなく長時
間溶接でき、チップの耐久性を向上させることができ
る。また、溶接による生産性を向上させることができ、
かつ適性溶接電流範囲も従来材と同レベルであり、溶接
性も良好である。(Advantages of the Invention) By doing so, in spot welding, the number of continuous spots can be increased, and welding can be performed for a long time without changing the tip, and the durability of the tip can be improved. In addition, productivity can be improved by welding,
Moreover, the suitable welding current range is the same level as the conventional material, and the weldability is also good.
更にプレスにおいて摺動性を冷延鋼板並以上に向上し、
かつ化成処理皮膜も形成可能とすることができる。これ
によって、従来より低コストで、またユーザーの工程に
おける負荷を低減でき、プレスによる生産性を向上させ
ることができるなどの優れた効果が得られる。Furthermore, in the press, the slidability is improved more than cold rolled steel sheet,
Moreover, a chemical conversion coating can be formed. As a result, it is possible to obtain excellent effects such as a lower cost than before, a load on a user's process can be reduced, and productivity by pressing can be improved.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 森田 順一 愛知県東海市東海町5―3 新日本製鐵株 式會社名古屋製鐵所内 (56)参考文献 特開 平4−21751(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Junichi Morita 5-3 Tokai-cho, Tokai City, Aichi Prefecture Nippon Steel Co., Ltd. Inside the Nippon Steel Works (56) Reference JP-A-4-21751 (JP, A)
Claims (2)
g/m2の酸化物、その上層にMn酸化物、P酸化物、Mo酸化
物、Co酸化物、Ni酸化物、Ca酸化物、W酸化物、V酸化
物あるいはホウ酸の1種または2種以上を1〜500mg/m2
(酸化物中の金属量として)を被覆してなることを特徴
とする溶接性、プレス性、化成処理性に優れた亜鉛系め
っき鋼板。1. The amount of ZnO on the surface of a galvanized steel sheet is 30 to 3000 m.
g / m 2 oxide, one or two of Mn oxide, P oxide, Mo oxide, Co oxide, Ni oxide, Ca oxide, W oxide, V oxide or boric acid as the upper layer 1 to 500 mg / m 2 for seeds or more
A zinc-based plated steel sheet having excellent weldability, pressability, and chemical conversion treatability, characterized by being coated (as the amount of metal in the oxide).
または2種以上を1〜500mg/m2含有せしめた請求項1に
記載の溶接性、プレス性、化成処理性に優れた亜鉛系め
っき鋼板。2. The weldability, pressability, and pressability according to claim 1, wherein the upper oxide layer contains 1 to 500 mg / m 2 of one or more of SiO 2 , TiO 2 , and Al 2 O 3 . A zinc-based plated steel sheet with excellent chemical conversion treatability.
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20285090A JPH0711070B2 (en) | 1990-07-31 | 1990-07-31 | Galvanized steel sheet with excellent weldability, pressability and chemical conversion treatment |
| PCT/JP1990/001615 WO1991009152A1 (en) | 1989-12-12 | 1990-12-11 | Galvanized steel plate having excellent capability of press working, chemical conversion and the like, and production of said plate |
| CA002046288A CA2046288C (en) | 1989-12-12 | 1990-12-11 | Zinc-base galvanized sheet steel excellent in press-formability, phosphatability, etc. and process for producing the same |
| KR1019910700888A KR940001032B1 (en) | 1989-12-12 | 1990-12-11 | Galvanized steel plate-having excellent capability of press working, chemical conversion and the like, and production of said plate |
| AU68889/91A AU629724B2 (en) | 1989-12-12 | 1990-12-11 | Deep drawing galvanised steel plate for press working and conversion coating |
| EP91900051A EP0456834B1 (en) | 1989-12-12 | 1990-12-11 | Galvanized steel plate having excellent capability of press working, chemical conversion and the like, and production of said plate |
| DE69027428T DE69027428T2 (en) | 1989-12-12 | 1990-12-11 | GALVANIZED STEEL SHEET WITH EXCELLENT PRESS FORMING, CHEMICAL SURFACE CONVERSION AND SIMILAR PROPERTIES AND THE PRODUCTION OF SUCH A SHEET |
| US08/108,937 US5525431A (en) | 1989-12-12 | 1993-08-19 | Zinc-base galvanized sheet steel excellent in press-formability, phosphatability, etc. and process for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20285090A JPH0711070B2 (en) | 1990-07-31 | 1990-07-31 | Galvanized steel sheet with excellent weldability, pressability and chemical conversion treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0488176A JPH0488176A (en) | 1992-03-23 |
| JPH0711070B2 true JPH0711070B2 (en) | 1995-02-08 |
Family
ID=16464230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20285090A Expired - Lifetime JPH0711070B2 (en) | 1989-12-12 | 1990-07-31 | Galvanized steel sheet with excellent weldability, pressability and chemical conversion treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0711070B2 (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07197277A (en) * | 1994-01-06 | 1995-08-01 | Nippon Steel Corp | Galvanized steel sheet with excellent spot weldability |
| JPH07197278A (en) * | 1994-01-06 | 1995-08-01 | Nippon Steel Corp | Galvanized steel sheet with excellent spot weldability |
| JP3273294B2 (en) * | 1995-02-13 | 2002-04-08 | 大阪市 | Electrolyte for zinc oxide film production |
| JPH08325688A (en) * | 1995-05-26 | 1996-12-10 | Nippon Steel Corp | Manufacturing facility for hot-dip galvanized steel sheets with excellent lubricity |
| JPH08325696A (en) * | 1995-05-26 | 1996-12-10 | Nippon Steel Corp | Manufacturing facility for hot-dip galvanized steel sheets with excellent lubricity |
| JPH08325689A (en) * | 1995-05-30 | 1996-12-10 | Nippon Steel Corp | Manufacturing facility for hot-dip galvanized steel sheet with excellent lubricity and chemical conversion treatment |
| JP3435255B2 (en) * | 1995-05-30 | 2003-08-11 | 新日本製鐵株式会社 | Manufacturing equipment for electro-galvanized steel sheet with excellent lubricity |
| JPH08325790A (en) * | 1995-05-31 | 1996-12-10 | Nippon Steel Corp | Manufacturing facility for galvanized hot-rolled steel sheets with excellent lubricity |
| JP5338195B2 (en) * | 2008-08-20 | 2013-11-13 | 新日鐵住金株式会社 | Surface-treated galvanized steel sheet and method for producing the same |
| JP6870338B2 (en) * | 2017-01-19 | 2021-05-12 | 日本製鉄株式会社 | Zn-Al plated steel sheet with excellent phosphate chemical conversion treatment and its manufacturing method |
| JP7842349B2 (en) * | 2023-03-23 | 2026-04-08 | 日本製鉄株式会社 | Zinc-plated steel sheet with excellent press formability, chemical treatment properties, and appearance quality, and method for manufacturing the same. |
-
1990
- 1990-07-31 JP JP20285090A patent/JPH0711070B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0488176A (en) | 1992-03-23 |
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