JP3063920B2 - How to treat metal surfaces with phosphate - Google Patents

How to treat metal surfaces with phosphate

Info

Publication number
JP3063920B2
JP3063920B2 JP3118012A JP11801291A JP3063920B2 JP 3063920 B2 JP3063920 B2 JP 3063920B2 JP 3118012 A JP3118012 A JP 3118012A JP 11801291 A JP11801291 A JP 11801291A JP 3063920 B2 JP3063920 B2 JP 3063920B2
Authority
JP
Japan
Prior art keywords
phosphate
metal surface
phosphate solution
solution containing
steel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP3118012A
Other languages
Japanese (ja)
Other versions
JPH04228579A (en
Inventor
ホルスト・ゲーメッカー
ベルナー・ラウシュ
ペーター・シューバッハ
Original Assignee
メタルゲゼルシャフト・アクチエンゲゼルシャフト
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=6405232&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JP3063920(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by メタルゲゼルシャフト・アクチエンゲゼルシャフト filed Critical メタルゲゼルシャフト・アクチエンゲゼルシャフト
Publication of JPH04228579A publication Critical patent/JPH04228579A/en
Application granted granted Critical
Publication of JP3063920B2 publication Critical patent/JP3063920B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/82After-treatment
    • C23C22/83Chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/18Orthophosphates containing manganese cations
    • C23C22/186Orthophosphates containing manganese cations containing also copper cations
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/18Orthophosphates containing manganese cations
    • C23C22/188Orthophosphates containing manganese cations containing also magnesium cations
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
    • C23C22/368Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing magnesium cations

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Treatment Of Metals (AREA)

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、亜鉛、マンガンおよび
リン酸の各イオンと、酸化剤とを含む酸性のリン酸塩水
溶液で金属表面を処理する方法、特に鋼、亜鉛メッキ
鋼、亜鉛合金メッキ鋼、アルミニウムおよびアルミニウ
ム合金の表面を上記水溶液にて処理する方法ならびに、
塗装、特に電着塗装の前処理として上記方法を使用する
方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating a metal surface with an aqueous solution of an acidic phosphate containing ions of zinc, manganese and phosphate and an oxidizing agent. Gold-plated steel, a method of treating the surface of aluminum and aluminum alloy with the above aqueous solution, and
It relates to the use of the above method as a pretreatment for painting, in particular for electrodeposition painting.

【0002】[0002]

【従来の技術】堅固に付着し、しかも本質的に耐食性を
向上させる働きのある金属リン酸塩皮膜を金属表面に生
成するため、金属はリン酸塩で処理される。なお上記皮
膜が、ペンキや他の有機皮膜と組合わされると、ペンキ
等の付着力や表面の耐食性が本質的に改善され得るであ
ろう。また上記金属リン酸塩皮膜は、電流の流れを妨げ
る絶縁体としても機能し、さらに潤滑剤と結びついてす
べり摩擦を軽減させる効果も有する。
BACKGROUND OF THE INVENTION Metals are treated with phosphates to form a metal phosphate coating on the metal surface that adheres firmly and essentially improves corrosion resistance. It should be noted that if the coating is combined with paint or another organic coating, the adhesion of paint and the like and the corrosion resistance of the surface could be substantially improved. The metal phosphate film also functions as an insulator that prevents the flow of current, and has an effect of reducing sliding friction by being combined with a lubricant.

【0003】ところで塗装前の前処理には、例えば0.
5ないし1.5g/lの比較的低濃度の亜鉛イオンを含
んだリン酸塩溶液を使用する低亜鉛リン酸塩皮膜形成法
が特に適している。そしてこの条件下では、フォスフォ
フィリット(PHOSPHOPHYLLIT;Zn2
e(PO4 2・4H2 O)含有量の高いリン酸塩皮膜
が鋼表面上に形成される。なおこのフォスフォフィリッ
トは、高亜鉛リン酸塩溶液から析出するホープアイト
(Hopeit;Zn3 Fe(PO4 2 ・4H2 O)
に較べてはるかに耐食性が高い。
[0003] By the way, the pre-treatment before coating includes, for example, 0.1.
Particularly suitable is a low zinc phosphate film formation method using a phosphate solution containing a relatively low concentration of zinc ions of 5 to 1.5 g / l. Under these conditions, the phosphofilit (PHOSPHOPHYLIT; Zn 2 F
A phosphate film with a high e (PO 4 ) 2 .4H 2 O) content is formed on the steel surface. In addition, this phosphofilite is formed by Hopeite (Zn 3 Fe (PO 4 ) 2 .4H 2 O) precipitated from a high zinc phosphate solution.
Corrosion resistance is much higher than

【0004】上記低亜鉛リン酸塩溶液が、ニッケルイオ
ンおよび/またはマンガンイオンを含有する場合には、
塗料膜と協働した防食効果は更に向上する。例えば0.
5ないし1.5g/lのマンガンイオンと、例えば0.
3ないし2.0g/lのニッケルイオンとを含む低亜鉛
リン酸塩処理法は、いわゆる三カチオン法として金属表
面の塗装前処理に、例えば自動車車体のカソード電着塗
装に広く応用されている。
When the low zinc phosphate solution contains nickel ions and / or manganese ions,
The anticorrosion effect in cooperation with the paint film is further improved. For example, 0.
5 to 1.5 g / l of manganese ions, e.g.
The low zinc phosphate treatment method containing 3 to 2.0 g / l of nickel ions is widely applied as a so-called trication method to a pretreatment for coating a metal surface, for example, to a cathode electrodeposition coating of an automobile body.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記三
カチオン法のリン酸塩溶液中にはニッケルイオンが高濃
度で存在すること、ならびに、形成されたリン酸塩皮膜
中に存在するニッケルおよびニッケル化合物の含有量の
高いことは、労働安全衛生および環境保全の見地からそ
の危険性が指摘されている。
However, the phosphate solution of the above-mentioned trication method contains a high concentration of nickel ions, and the nickel and nickel compounds present in the formed phosphate film. It has been pointed out that the high content of this substance is dangerous from the viewpoint of occupational safety and health and environmental protection.

【0006】本発明の解決すべき課題は、品質において
はZn─Mn−Niを主剤とする上記三カチオン法によ
る皮膜に匹敵するが、ニッケルおよびニッケル化合物の
存在による欠点を有しないリン酸塩皮膜形成をもたらす
リン酸塩処理法、特に鋼、亜鉛メッキ鋼、亜鉛合金メッ
キ鋼、アルミニウムならびにアルミニウム合金のごとき
金属のリン酸塩処理法を提供することにある。
The problem to be solved by the present invention is that the phosphate film which is comparable in quality to the film formed by the above-mentioned trication method using Zn @ Mn-Ni as a main component, but does not have the drawbacks caused by the presence of nickel and a nickel compound. It is an object of the present invention to provide a phosphating method which results in the formation of a metal, such as steel, galvanized steel, galvanized steel, aluminum and aluminum alloys.

【0007】[0007]

【課題を解決するための手段】この課題は、当初に述べ
た皮膜形成法を次のような形に発展させた本発明により
解決することができる。すなわちこの方法では基本的に
ニッケルを含まず、 0.3 ないし 1.7 g/l Zn 0.2 ないし 4.0 g/l Mn 0.001 ないし 0.030 g/l Cu 5 ないし 30 g/l リン
酸塩(P2 5 換算) を含み、酸素および/または同様な効果を有する他の酸
化剤を用いて液中のFe(II)濃度を0.1g/l以
下に保持すると共に、pH値を3.0ないし3.8に調
整したリン酸塩溶液に金属表面は接触させられる。
This problem can be solved by the present invention in which the above-described film forming method is developed into the following form. That is, this method basically does not contain nickel, and contains 0.3 to 1.7 g / l Zn 0.2 to 4.0 g / l Mn 0.001 to 0.030 g / l Cu 5 to 30 g / l 1 containing phosphate (in terms of P 2 O 5 ), maintaining the Fe (II) concentration in the solution at 0.1 g / l or less using oxygen and / or another oxidizing agent having a similar effect, The metal surface is contacted with a phosphate solution whose pH has been adjusted to between 3.0 and 3.8.

【0008】本発明による方法は、特に鋼、亜鉛メッキ
鋼、亜鉛合金メッキ鋼、アルミニウムおよびアルミニウ
ム合金に適用される。ここでいう鋼の概念には、非合金
軟鋼、準高張力および高張力鋼(例えば、ミクロ合金化
鋼(mikrolegiert)、二相鋼(Dual−
Phase)およびリン合金化鋼)および低合金鋼が含
まれる。なお、亜鉛メッキ層は、例えば、電解、溶融浸
せきまたは蒸着によって作られる。
The method according to the invention applies in particular to steel, galvanized steel, galvanized steel, aluminum and aluminum alloys. As used herein, the concept of steel includes non-alloyed mild steel, semi-high tensile and high tensile steel (e.g., microalloyed steel (mikrolegiert), duplex stainless steel (Dual-
Phase) and phosphorus alloyed steels) and low alloy steels. The galvanized layer is formed by, for example, electrolysis, melt immersion, or vapor deposition.

【0009】ここでいう亜鉛の典型的な品質は、純亜鉛
と、例えばFe、Ni、Co、Al、Crを含む合金と
から成る。またここで言うアルミニウムおよびその合金
は、金属工業で使用される鋳造および鍛造用材料を意味
し、合金成分として、例えば、Mg、Mn、Cu、S
i、Zn、Fe、Cr、Ni、Tiを含有している。
The typical quality of zinc here is pure zinc and an alloy containing, for example, Fe, Ni, Co, Al and Cr. Also, the aluminum and its alloys referred to herein refer to casting and forging materials used in the metal industry, and include, for example, Mg, Mn, Cu, S
It contains i, Zn, Fe, Cr, Ni and Ti.

【0010】本発明の方法にとって基本的に必要な要件
は、酸性のリン酸塩溶液が原理的にニッケルを含まない
ことである。これは工業的な条件下で、リン酸塩溶液中
のニッケル濃度が0.0002ないし0.01g/l以
下であることを意味する。しかしながら、0.0001
g/l以下であることが好ましい。
A fundamental requirement for the process according to the invention is that the acidic phosphate solution is essentially free of nickel. This means that under industrial conditions the nickel concentration in the phosphate solution is from 0.0002 to 0.01 g / l. However, 0.0001
g / l or less.

【0011】本発明のその他の本質的な特徴としては、
三種の金属イオン、Zn、Mn、Cuが前記濃度で存在
することが挙げられる。そして特に鋼を処理する場合、
Zn濃度を0.3g/l以下にすると皮膜形成が悪化す
る。Zn濃度を1.7g/l以上にすると、鋼表面に形
成されるリン酸塩皮膜中のフォスフォフィリット含量が
大幅に減少する。またかくして生じたリン酸塩皮膜がペ
ンキと組合わされると、極めて低い品質を示すことにな
る。
[0011] Other essential features of the present invention include:
Three types of metal ions, Zn, Mn, and Cu, may be present at the above concentrations. And especially when processing steel
When the Zn concentration is 0.3 g / l or less, the film formation deteriorates. When the Zn concentration is 1.7 g / l or more, the content of the phosphofilite in the phosphate film formed on the steel surface is greatly reduced. Also, when the resulting phosphate film is combined with paint, it will exhibit very poor quality.

【0012】次にMn濃度が0.2g/l以下の場合に
は、このカチオンを添加する利点は見受けられない。ま
た濃度を4g/l以上にしても、なお一層の品質向上は
観測されない。さらにCu濃度は0.001ないし0.
030g/lであるが、0.001以下では皮膜の形成
および皮膜の質にとって好ましい効果が失われ、他方、
0.030g/l以上では、有害なCuセメンテーショ
ンが増大する。
When the Mn concentration is 0.2 g / l or less, there is no advantage in adding this cation. Even when the concentration is 4 g / l or more, no further improvement in quality is observed. Further, the Cu concentration is 0.001 to 0.5.
030 g / l, but if it is 0.001 or less, favorable effects on film formation and film quality are lost.
Above 0.030 g / l, harmful Cu cementation increases.

【0013】リン酸塩皮膜を鋼に形成する場合、Feは
Fe(II)の形で溶液中に移行する。したがってリン
酸塩処理浴は、Fe(II)イオンの定常的濃度が0.
1g/lを越えないようにするため、充分な酸素および
/または他の酸化物を含有していなければならない。す
なわち、それ以上のFeはFe(III)に転化され、
リン酸鉄スラッジとして沈澱することになる。
When a phosphate film is formed on steel, Fe migrates into solution in the form of Fe (II). Therefore, the phosphating bath has a steady concentration of Fe (II) ions of 0,1.
Sufficient oxygen and / or other oxides must be contained in order not to exceed 1 g / l. That is, more Fe is converted to Fe (III),
It will precipitate as iron phosphate sludge.

【0014】完璧なリン酸塩皮膜を確実に形成しようと
すれば、リン酸塩溶液のpH値は、3.0ないし3.8
に調整しなけばならない。そして高目のpH値は、浴温
度が低目の場合か、浴濃度が低目の場合に選択され、低
目のpH値は、浴温度が高目の場合か、浴濃度が高目の
場合に選択されるであろう。
To ensure that a perfect phosphate film is formed, the pH of the phosphate solution should be between 3.0 and 3.8.
Have to be adjusted. The higher pH value is selected when the bath temperature is lower or the bath concentration is lower. The lower pH value is selected when the bath temperature is higher or the bath concentration is higher. Will be selected in case.

【0015】次にこのpH値の調整に必要とあれば、別
のカチオン、たとえば、アルカリ金属イオン(Na、
K、NH4 その他)および/またはアルカリ土金属イオ
ン(Mg、Ca)および別のアニオン(NO3 、Cl、
SiF6 、SO4 、BF4 その他)がリン酸塩溶液に添
加されてもよい。
Next, if necessary for adjusting the pH value, another cation such as an alkali metal ion (Na,
K, NH 4 and others) and / or alkaline earth metal ions (Mg, Ca) and another anion (NO 3 , Cl,
SiF 6 , SO 4 , BF 4 etc.) may be added to the phosphate solution.

【0016】また上記リン酸塩溶液のpH値は、液の準
備中や使用中に、必要なら塩基性化合物(NaOH、N
2 CO3 、ZnO、ZnCO3 、MnCO3 その他)
または酸(HNO3 、H3 PO4 、H2 SiF6 、HC
lその他)を添加して調整してもよい。
The pH value of the above phosphate solution may be adjusted during preparation or use of the solution, if necessary, with a basic compound (NaOH, N
a 2 CO 3 , ZnO, ZnCO 3 , MnCO 3 etc.)
Or acid (HNO 3 , H 3 PO 4 , H 2 SiF 6 , HC
1) may be added for adjustment.

【0017】ところで3g/l以下のMgおよび/また
はCaを上記リン酸塩溶液に添加することにより、上記
リン酸塩皮膜の質を改善することができる。またその場
合の最適濃度は、0.4ないし1.3g/lの範囲にあ
るのがよい。なおこれらのカチオンは、リン酸塩または
前記アニオン塩の形でリン酸塩溶液中に添加するのがよ
い。このほか、酸化物、水酸化物、炭酸塩も、Mgまた
はCa源として使用することができる。
The quality of the phosphate film can be improved by adding 3 g / l or less of Mg and / or Ca to the phosphate solution. The optimum concentration in that case is preferably in the range of 0.4 to 1.3 g / l. These cations are preferably added to the phosphate solution in the form of a phosphate or the above-mentioned anion salt. In addition, oxides, hydroxides, and carbonates can also be used as Mg or Ca sources.

【0018】次に上記リン酸塩溶液をスプレー方式にて
使用する場合、Zn濃度は0.3ないし1g/lである
のが好ましい。またスプレーと浸せきとの併用方式、ま
たは浸せき方式にて使用する場合は、Zn濃度は0.9
ないし1.7g/lであるのが好ましい。なお好ましい
Mn濃度は、上記諸方式に関係なく0.4ないし1.3
g/lであるのがよい。
Next, when the above phosphate solution is used by a spray method, the Zn concentration is preferably 0.3 to 1 g / l. When used in combination with spray and dipping, or dipping, the Zn concentration is 0.9.
To 1.7 g / l. The preferred Mn concentration is 0.4 to 1.3 regardless of the above-mentioned methods.
g / l.

【0019】次に上記リン酸塩溶液中のCuは、0.0
03ないし0.020g/lの範囲にあるが、0.00
3ないし0.020g/lの範囲にあるのがよい。特に
良好なリン酸塩皮膜を得るためには、CuとP2 5
の重量比が1:(5ないし2000)で補給されるとき
であろう。
Next, Cu in the above phosphate solution is 0.0%
03 to 0.020 g / l, but 0.00
It is preferably in the range of 3 to 0.020 g / l. A particularly good phosphate film will be obtained when the weight ratio of Cu to P 2 O 5 is replenished at 1: (5 to 2000).

【0020】次にFe(II)濃度を制限するため、リ
ン酸塩溶液には酸素、例えば大気中の酸素との接触、お
よび/または適当な酸化剤の添加が行われる。この酸化
剤としては、亜硝酸塩、塩素酸塩、臭素酸塩、ペルオキ
シ化合物(H2 2 、過ホウ酸塩、過炭酸塩、過リン酸
塩その他)および有機ニトロ化合物、例えばニトロベン
ゼンスルホネートが好ましい。
The phosphate solution is then contacted with oxygen, for example atmospheric oxygen, and / or with the addition of a suitable oxidizing agent in order to limit the Fe (II) concentration. As the oxidizing agent, nitrite, chlorate, bromate, peroxy compounds (H 2 O 2 , perborate, percarbonate, perphosphate and the like) and organic nitro compounds such as nitrobenzene sulfonate are preferable. .

【0021】またこれらの酸化剤は単体で、あるいは組
合せて使用されるが、場合によっては硝酸塩のような比
較的弱い酸化剤と併用されることもある。適した組合せ
は、例えば、亜硝酸塩と硝酸塩、亜硝酸塩と塩素酸塩
(又は硝酸塩)、ペルオキシ化合物とNO3 、臭素酸塩
と硝酸塩、塩素酸塩とニトロベンゼンスルホネート(硝
酸塩)である。なお上記酸化剤は、Fe(II)イオン
の酸化に役立つだけではなく、リン酸塩皮膜の形成をも
促進する効果も有する。
These oxidizing agents may be used alone or in combination, but may be used in combination with a relatively weak oxidizing agent such as nitrate. Suitable combinations are, for example, nitrite and nitrate, nitrite and chlorate (or nitrate), peroxy compounds and NO 3 , bromate and nitrate, chlorate and nitrobenzenesulfonate (nitrate). Note that the oxidizing agent not only serves to oxidize Fe (II) ions, but also has an effect of promoting formation of a phosphate film.

【0022】ところで上記の酸化剤のリン酸塩処理浴中
における典型的な濃度は、亜硝酸塩:0.04ないし
0.5g/l;塩素酸塩:0.5ないし5g/l;臭素
酸塩:0.3ないし4g/l;ペルオキシ化合物(H2
2換算):0.005ないし0.1g/l;ニトロベ
ンゼンスルホネート:0.05ないし1g/lの範囲に
ある。
The typical concentrations of the above oxidizing agents in the phosphating bath are: nitrite: 0.04 to 0.5 g / l; chlorate: 0.5 to 5 g / l; : 0.3 to 4 g / l; peroxy compound (H 2
O 2 equivalent): 0.005 to 0.1 g / l; nitrobenzenesulfonate: in the range of 0.05 to 1 g / l.

【0023】次に金属表面は、付加的修正作用を持つグ
ループの化合物を添加したリン酸塩溶液で処理されるの
が好ましい。なおこのグループは、界面活性剤、ヒドロ
キシカルボン酸、酒石酸塩、クエン酸塩、単純フッ化
物、ホウフッ化物、ケイフッ化物から成る。
The metal surface is then preferably treated with a phosphate solution to which a group of compounds having an additional modifying action has been added. This group consists of surfactants, hydroxycarboxylic acids, tartrate salts, citrate salts, simple fluorides, borofluorides and silicofluorides.

【0024】上記グループのうち界面活性剤(例えば
0.05ないし0.5g/l)の添加は、軽度に油が塗
布された金属表面のリン酸塩皮膜の形成を改善する。ま
たヒドロキシカルボン酸、例えば酒石酸、クエン酸およ
びそれらの塩は、例えば0.03ないし0.3g/lの
濃度範囲で、リン酸塩皮膜重量の顕著な減少をもたら
す。
The addition of a surfactant (eg 0.05 to 0.5 g / l) from the above group improves the formation of a phosphate film on lightly oiled metal surfaces. Also, hydroxycarboxylic acids such as tartaric acid, citric acid and their salts, for example, in the concentration range of 0.03 to 0.3 g / l, lead to a significant reduction in phosphate coating weight.

【0025】さらに単純フッ化物は比較的難腐食性のリ
ン酸塩皮膜の形成を促進し、しかもその際、リン酸塩皮
膜処理の最小所要時間を短縮し、またリン酸塩皮膜の表
面掩蔽率をも高める。なおこの目的のためには、例えば
0.1ないし1g/lのF濃度が適当である。
In addition, simple fluorides promote the formation of phosphate coatings which are relatively hard to corrode, while also reducing the minimum time required for phosphate coating treatment, and the surface coverage of the phosphate coating. Also enhance. For this purpose, an F concentration of, for example, 0.1 to 1 g / l is appropriate.

【0026】この単純フッ化物は、その添加を管理する
ことによって、アルミニウムおよびその合金上に結晶性
のリン酸塩皮膜を形成することができる。なおBF4
よびSiF6 も、リン酸塩皮膜処理浴の攻撃性(Aggres
sivitaet)を高めるが、これは特に乾式亜鉛メッキ表面
の処理の際に明瞭に現れる。この場合の添加量は例えば
0.4ないし3g/lであるのがよい。
By controlling the addition of this simple fluoride, a crystalline phosphate film can be formed on aluminum and its alloys. BF 4 and SiF 6 are also aggressive (Aggres
sivitaet), which is particularly apparent during the treatment of dry galvanized surfaces. In this case, the amount added is, for example, preferably 0.4 to 3 g / l.

【0027】ところで本発明に係るリン酸塩溶液は、ス
プレー、スプレーと浸せき、または浸せきによって金属
表面に施される。また浴温度は、通常40ないし60℃
の範囲に保たれる。さらに処理時間については、鋼およ
びアルミニウムの場合、均一被覆のリン酸塩皮膜を析出
させるために1ないし5分で充分である。他方亜鉛メッ
キ鋼の場合は、しばしば10秒以下で充分である。した
がって本発明の方法は、帯状体を高速で送る設備にも使
用することができる。
The phosphate solution of the present invention is applied to a metal surface by spraying, spraying and dipping, or dipping. The bath temperature is usually 40 to 60 ° C.
Is kept in the range. In addition, in the case of steel and aluminum, a treatment time of 1 to 5 minutes is sufficient for depositing a uniformly coated phosphate film. On the other hand, in the case of galvanized steel, less than 10 seconds is often sufficient. Therefore, the method of the present invention can also be used for equipment for feeding a strip at a high speed.

【0028】金属表面は、リン酸塩溶液で処理される前
に、一般に洗浄され、すすがれ、およびリン酸チタンを
主剤とする活性化剤にて処理されることが多い。
Before being treated with the phosphate solution, the metal surface is generally washed, rinsed and often treated with an activator based on titanium phosphate.

【0029】本発明のリン酸塩皮膜形成法により作られ
たリン酸塩皮膜層は、微結晶性で、しかも均一な厚さを
有する。またその単位表面当たり重量は、鋼、亜鉛メッ
キ鋼および亜鉛合金メッキ鋼を処理した場合、1.5な
いし4.5g/m2 、アルミニウムおよびその合金を処
理した場合、0.5ないし2.5g/m2 であることが
多い。
The phosphate film formed by the phosphate film forming method of the present invention is microcrystalline and has a uniform thickness. The weight per unit surface is 1.5 to 4.5 g / m 2 for steel, galvanized steel and zinc alloy-plated steel, and 0.5 to 2.5 g for aluminum and its alloys. / M 2 .

【0030】上記リン酸塩溶液の組成は、例えばリン酸
塩皮膜の生成、スラッジの発生、処理された金属表面に
溶液が残留することによる機械的損失、スラッジを除去
する際の機械的損失、あるいは酸化還元反応および分解
によって、リン酸塩処理の実施中に消費される。このた
めリン酸塩処理浴は分析化学的に監視されると共に、不
足成分は補充されなければならない。
The composition of the phosphate solution may be, for example, the formation of a phosphate film, the generation of sludge, the mechanical loss due to the solution remaining on the treated metal surface, the mechanical loss in removing sludge, Alternatively, it is consumed during the phosphating process by redox reaction and decomposition. For this reason, the phosphating bath must be monitored analytically and any missing components must be replenished.

【0031】上記リン酸塩皮膜は、とり分け、防食のた
め、切削を伴わない冷間加工を容易にするためおよび、
電気的な絶縁を得るために有効に使用することができ
る。さらに、このリン酸塩皮膜は、金属表面の塗装、特
に電着塗装の前処理に好んで使用される。そしてカソー
ド電着塗装と組合されるとき、特に良好な成績が得られ
る。
The above-mentioned phosphate film is used, in particular, for corrosion protection, to facilitate cold working without cutting, and
It can be used effectively to obtain electrical insulation. Furthermore, the phosphate coating is preferably used for painting metal surfaces, especially for pretreatment of electrodeposition coating. And particularly good results are obtained when combined with cathodic electrodeposition coating.

【0032】上記リン酸塩皮膜は、上記塗装の前に例え
ばCr(VI)、Cr(VI)─Cr(III)、Cr
(III)、Cr(III)─フルオロジルコニウム錯
塩、Al(III)、Al(III)─フロオロジルコ
ニウム錯塩を主剤とした不働態化性すすぎ剤で処理する
ことが推奨される。これによって塗膜の付着性や、耐腐
食浸透性がさらに向上するであろう。
Prior to the coating, the phosphate film is made of, for example, Cr (VI), Cr (VI) ─Cr (III),
It is recommended to treat with a passivating rinsing agent based on (III), Cr (III) ─fluorozirconium complex, Al (III), Al (III) ─fluorodisilconium complex. This will further improve the adhesion of the coating and the corrosion penetration resistance.

【0033】[0033]

【実施例】先づ鋼、亜鉛メッキ鋼、およびアルミニウム
の各薄板は、アルカリ性洗浄剤で脱脂された。
EXAMPLE First, steel, galvanized steel, and aluminum sheets were degreased with an alkaline cleaner.

【0034】次に水ですすぎ洗いをされ、さらに必要な
場合には、活性化のためにリン酸チタン含有溶液による
前処理が行われ、そのあと温度50℃でリン酸塩皮膜が
形成された。その際使用されたリン酸塩溶液は、表1に
示す12種類である。
Next, a rinse with water was carried out and, if necessary, a pretreatment with a titanium phosphate-containing solution was carried out for activation, after which a phosphate film was formed at a temperature of 50 ° C. . The phosphate solutions used at that time are 12 types shown in Table 1.

【0035】 注) NBS:ニトロベンゼンスルホネート・ナトリウ
ム塩全酸量:浴サンプル10ml当たりの0.1N N
aOH消費量ml(フ なお凡ての浴についてFe(II)濃度は0.1g/l
であった。
[0035] Note) NBS: Total acid amount of nitrobenzenesulfonate / sodium salt: 0.1 N N per 10 ml of bath sample
aOH consumption ml (F The Fe (II) concentration for all baths was 0.1 g / l.
Met.

【0036】表から凡ての試験例で、均一厚さのリン酸
塩皮膜が得られたことがわかる。なおこのリン酸塩皮膜
は、カソード電着塗装や、自動車工業で行うような塗装
と結合されると、高い耐食性や耐腐食浸透性を示すこと
が判明した。
From the table, it can be seen that in all the test examples, a phosphate film having a uniform thickness was obtained. It has been found that this phosphate coating exhibits high corrosion resistance and corrosion penetration resistance when combined with cathodic electrodeposition coating and coatings such as those performed in the automotive industry.

【0037】[0037]

【発明の効果】本発明は上述のような構成であるから、
処理溶液中にニッケルが含まれない。また形成されたリ
ン酸塩皮膜中にもニッケルは存在しない。
Since the present invention has the above configuration,
There is no nickel in the processing solution. Also, nickel does not exist in the formed phosphate film.

【0038】したがって労働安全衛生上および環境保全
上、危険が全くないだけでなく、本発明の方法で形成さ
れるリン酸塩皮膜は、その品質が従来のそれに較べて全
くそん色がない。
Therefore, not only is there no danger in terms of occupational safety and health and environmental protection, but also the phosphate film formed by the method of the present invention has no color at all in comparison with the conventional one.

フロントページの続き (72)発明者 ベルナー・ラウシュ ドイツ連邦共和国6370オーバーウルゼ ル、ウルゼーマーシュトラーセ43 (72)発明者 ペーター・シューバッハ ドイツ連邦共和国6369シェーネック−オ ーバードルフェルデン、イム・グリュン トヒェン14 (56)参考文献 特開 平3−87374(JP,A) 特開 昭59−110785(JP,A) 特開 平3−61385(JP,A) (58)調査した分野(Int.Cl.7,DB名) C23C 22/00 - 22/86 Continued on the front page (72) Inventor Berner Rausch, Germany 6370 Oberursel, Urseemerstraße 43 (72) Inventor Peter Schübach, Germany 6369 Schöneck-Oberdorfelden, Im Grün-Tchen 14 (56) References JP-A-3-87374 (JP, A) JP-A-59-110785 (JP, A) JP-A-3-61385 (JP, A) (58) Fields studied (Int. 7 , DB name) C23C 22/00-22/86

Claims (11)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】亜鉛、マンガンおよびリン酸の各イオン
と、酸化剤とを含む酸性のリン酸塩水溶液で金属表面を
処理する方法において、基本的にニッケルを含まず、 0.3 ないし 1.7 g/l Zn 0.2 ないし 4.0 g/l Mn 0.001 ないし 0.030 g/l Cu 5 ないし 30 g/l リン
酸塩(P2 5 換算) を含み、酸素および/または同様な効果を有する他の酸
化剤を用いて液中のFe(II)濃度を0.1g/l以
下に保持すると共に、pH値を3.0ないし3.8に調
整したリン酸塩溶液で金属表面を処理する方法。
1. A method for treating a metal surface with an aqueous acidic phosphate solution containing ions of zinc, manganese and phosphoric acid and an oxidizing agent, wherein the method is essentially free of nickel, and contains 0.3 to 1. Contains 7 g / l Zn 0.2 to 4.0 g / l Mn 0.001 to 0.030 g / l Cu 5 to 30 g / l phosphate (in terms of P 2 O 5 ), and contains oxygen and / or Using another oxidizing agent having a similar effect, the Fe (II) concentration in the solution is kept at 0.1 g / l or less, and the pH value is adjusted to 3.0 to 3.8 with a phosphate solution. A method for treating metal surfaces.
【請求項2】3g/l以下、好ましくは、0.4ないし
1.3g/lのMgおよび/またはCaを追加的に含有
させたリン酸塩溶液で金属表面を処理する請求項1記載
の方法。
2. The metal surface according to claim 1, wherein the metal surface is treated with a phosphate solution additionally containing up to 3 g / l, preferably 0.4 to 1.3 g / l of Mg and / or Ca. Method.
【請求項3】0.3ないし1.0g/lのZnを含有さ
せたリン酸塩溶液に金属表面をスプレー方式で接触させ
ることを特徴とする請求項1または2記載の方法。
3. The method according to claim 1, wherein the metal surface is contacted with a phosphate solution containing 0.3 to 1.0 g / l of Zn by spraying.
【請求項4】0.9ないし1.7g/lのZnを含有さ
せたリン酸塩溶液に金属表面をスプレーと浸せきとの併
用方式で接触させることを特徴とする請求項1または2
記載の方法。
4. The method according to claim 1, wherein the metal surface is brought into contact with a phosphate solution containing 0.9 to 1.7 g / l of Zn by a combination of spraying and dipping.
The described method.
【請求項5】0.4ないし1.3g/lのMnを含有さ
せたリン酸塩溶液で金属表面を処理することを特徴とす
る請求項1、2、3または4記載の方法。
5. The method according to claim 1, wherein the metal surface is treated with a phosphate solution containing 0.4 to 1.3 g / l of Mn.
【請求項6】0.003ないし0.020g/lのCu
を含有させたリン酸塩溶液で金属表面を処理することを
特徴とする請求項1、2、3、4または5記載の方法。
6. 0.003 to 0.020 g / l of Cu
The method according to claim 1, 2, 3, 4, or 5, wherein the metal surface is treated with a phosphate solution containing.
【請求項7】Cuとリン酸塩(P2 5 換算)との重量
比は1:(170ないし30000)でありかつCuお
よびP2 5 は重量比1:(5ないし2000)で補給
される請求項1、2、3、4、5または6記載の方法。
7. The weight ratio of Cu to phosphate (in terms of P 2 O 5 ) is 1: (170 to 30,000) and Cu and P 2 O 5 are supplied in a weight ratio of 1: (5 to 2,000). 7. The method of claim 1,2,3,4,5 or 6, wherein said method is performed.
【請求項8】亜硝酸塩、塩素酸塩、臭素酸塩、ペルオキ
シ化合物、ニトロベンゼンスルホネートのような有機ニ
トロ化合物を酸化剤として含有させたリン酸塩溶液に金
属表面を接触させることを特徴とする請求項1、2、
3、4、5、6または7記載の方法。
8. The metal surface is brought into contact with a phosphate solution containing an organic nitro compound such as nitrite, chlorate, bromate, peroxy compound, or nitrobenzene sulfonate as an oxidizing agent. Terms 1, 2,
The method according to 3, 4, 5, 6 or 7.
【請求項9】界面活性剤、ヒドロキシカルボン酸、酒石
酸塩、クエン酸塩、単純フッ化物、ホウフッ化物、ケイ
フッ化物のグループに属して付加的修正作用を有する化
合物を含有させたリン酸塩溶液に金属表面を接触させる
ことを特徴とする請求項1、2、3、4、5、6、7ま
たは8記載の方法。
9. A phosphate solution containing a compound belonging to the group of surfactants, hydroxycarboxylic acids, tartrate salts, citrate salts, simple fluorides, borofluorides and silicofluorides, which has an additional modifying action. The method according to claim 1, 2, 3, 4, 5, 6, 7, or 8, wherein the metal surface is brought into contact.
【請求項10】塗装、特に電着塗装される金属表面の前
処理に請求項1〜9記載の方法の1つを使用する方法。
10. Use of one of the methods according to claims 1 to 9 for the pretreatment of a metal surface to be coated, especially for electrodeposition coating.
【請求項11】鋼、亜鉛メッキ鋼、亜鉛合金メッキ鋼、
アルミニウムおよびアルミニウム合金をリン酸塩で処理
する際に請求項1〜9記載の方法の1つを使用する方
法。
11. A steel, galvanized steel, zinc alloy-plated steel,
10. Use of one of the methods of claims 1 to 9 in treating aluminum and aluminum alloys with phosphate.
JP3118012A 1990-04-27 1991-04-22 How to treat metal surfaces with phosphate Expired - Lifetime JP3063920B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4013483A DE4013483A1 (en) 1990-04-27 1990-04-27 METHOD FOR PHOSPHATING METAL SURFACES
DE4013483.0 1990-04-27

Publications (2)

Publication Number Publication Date
JPH04228579A JPH04228579A (en) 1992-08-18
JP3063920B2 true JP3063920B2 (en) 2000-07-12

Family

ID=6405232

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3118012A Expired - Lifetime JP3063920B2 (en) 1990-04-27 1991-04-22 How to treat metal surfaces with phosphate

Country Status (11)

Country Link
EP (1) EP0459541B1 (en)
JP (1) JP3063920B2 (en)
BR (1) BR9101660A (en)
CA (1) CA2039901C (en)
CZ (1) CZ281471B6 (en)
DE (2) DE4013483A1 (en)
ES (1) ES2081420T3 (en)
MX (1) MX172859B (en)
PL (1) PL166676B1 (en)
RU (1) RU2051988C1 (en)
ZA (1) ZA913133B (en)

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4210513A1 (en) 1992-03-31 1993-10-07 Henkel Kgaa Nickel-free phosphating process
JPH05287549A (en) * 1992-04-03 1993-11-02 Nippon Paint Co Ltd Zinc phosphate treatment on metallic surface for cation type electrodeposition coating
DE4214992A1 (en) * 1992-05-06 1993-11-11 Henkel Kgaa Copper-containing nickel-free phosphating process
DE4232292A1 (en) * 1992-09-28 1994-03-31 Henkel Kgaa Process for phosphating galvanized steel surfaces
DE4243214A1 (en) * 1992-12-19 1994-06-23 Metallgesellschaft Ag Process for the production of phosphate coatings
CA2150545A1 (en) * 1992-12-22 1994-07-07 Robert W. Miller Substantially nickel-free phosphate conversion coating composition and process
ATE162233T1 (en) * 1993-09-06 1998-01-15 Henkel Kgaa NICKEL-FREE PHOSPHATING PROCESS
FR2724395B1 (en) * 1994-09-12 1996-11-22 Gec Alsthom Transport Sa INSULATED MAGNETIC SHEET AND METHOD FOR ISOLATING SAME
DE4440300A1 (en) * 1994-11-11 1996-05-15 Metallgesellschaft Ag Process for applying phosphate coatings
NO312911B1 (en) * 1994-12-22 2002-07-15 Budenheim Rud A Oetker Chemie Anti-corrosion pigment and its use
DE19500927A1 (en) * 1995-01-16 1996-07-18 Henkel Kgaa Lithium-containing zinc phosphating solution
DE19511573A1 (en) * 1995-03-29 1996-10-02 Henkel Kgaa Process for phosphating with metal-containing rinsing
DE19606017A1 (en) * 1996-02-19 1997-08-21 Henkel Kgaa Zinc phosphating with low copper and manganese contents
DE19634732A1 (en) * 1996-08-28 1998-03-05 Henkel Kgaa Zinc phosphating containing ruthenium
AU9156398A (en) 1997-08-06 1999-03-01 Henkel Kommanditgesellschaft Auf Aktien Phosphating method accelerated by n-oxides
US6720032B1 (en) 1997-09-10 2004-04-13 Henkel Kommanditgesellschaft Auf Aktien Pretreatment before painting of composite metal structures containing aluminum portions
DE19740953A1 (en) * 1997-09-17 1999-03-18 Henkel Kgaa High speed spray or dip phosphating of steel strip
JPH11264076A (en) * 1998-01-14 1999-09-28 Nippon Paint Co Ltd Chemical conversion treatment for low lead ed
DE19808755A1 (en) 1998-03-02 1999-09-09 Henkel Kgaa Layer weight control for strip phosphating
DE10006338C2 (en) * 2000-02-12 2003-12-04 Chemetall Gmbh Process for coating metal surfaces, aqueous concentrate therefor and use of the coated metal parts
DE10110834B4 (en) * 2001-03-06 2005-03-10 Chemetall Gmbh Process for coating metallic surfaces and use of the substrates coated in this way
JP2002266080A (en) * 2001-03-07 2002-09-18 Nippon Paint Co Ltd Phosphate chemical conversion treatment solution, chemical conversion treatment method and chemical conversion treated steel sheet
DE102005047424A1 (en) * 2005-09-30 2007-04-05 Henkel Kgaa Phosphating solution used as a pre-treatment for metal surfaces contains zinc irons, phosphate ions, hydrogen peroxide or an equivalent amount of a hydrogen peroxide-splitting substance and aliphatic chelate-forming carboxylic acid
EP2336391B1 (en) 2008-10-08 2016-03-30 Nippon Steel & Sumitomo Metal Corporation Metal material having excellent corrosion resistance
RU2572688C1 (en) * 2014-09-10 2016-01-20 Закрытое акционерное общество "ФК" Solution for metal surface phosphating
EP4382641A1 (en) * 2022-12-07 2024-06-12 Henkel AG & Co. KGaA Method for electrolytic deposition of a phosphate layer on zinc surfaces
WO2024149790A1 (en) * 2023-01-11 2024-07-18 Chemetall Gmbh Composition for phosphatizing of ferrous surfaces and method making use thereof

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB526815A (en) * 1939-03-14 1940-09-26 Samuel Thomas Roberts Improvements relating to the rustproofing of ferrous surfaces prior to painting or enamelling
US2813812A (en) * 1952-06-24 1957-11-19 Parker Rust Proof Co Method for coating iron or zinc with phosphate composition and aqueous solution therefor
DE1223657B (en) * 1961-08-09 1966-08-25 Chemische Und Lackfabrik Process for phosphating metal surfaces
DE1287413B (en) * 1965-11-06 1969-01-16 Metallgesellschaft Ag Process for preparing steel for electrophoretic coating with paints
IT975560B (en) * 1972-10-20 1974-08-10 Sec Accomandita Semplice Fosfa PROCEDURE FOR PHOSPHATING ON METALLIC SURFACES INTENDED FOR PAINTING ESPECIALLY FOR ELETROPHORESIS AND SOLUTION RELATING TO THIS PROCEDURE
DE3345498A1 (en) * 1983-12-16 1985-06-27 Metallgesellschaft Ag, 6000 Frankfurt Process for producing phosphate coatings

Also Published As

Publication number Publication date
CA2039901C (en) 2000-11-14
ES2081420T3 (en) 1996-03-16
CA2039901A1 (en) 1991-10-28
JPH04228579A (en) 1992-08-18
CZ118091A3 (en) 1994-04-13
BR9101660A (en) 1991-11-26
EP0459541A1 (en) 1991-12-04
DE4013483A1 (en) 1991-10-31
MX172859B (en) 1994-01-17
EP0459541B1 (en) 1995-11-22
ZA913133B (en) 1992-12-30
CZ281471B6 (en) 1996-10-16
RU2051988C1 (en) 1996-01-10
PL166676B1 (en) 1995-06-30
DE59106926D1 (en) 1996-01-04
PL290031A1 (en) 1992-02-24

Similar Documents

Publication Publication Date Title
JP3063920B2 (en) How to treat metal surfaces with phosphate
JP4427332B2 (en) Treatment liquid for surface treatment of aluminum or magnesium metal and surface treatment method
EP0315059B1 (en) Process and composition for zinc phosphate coating
RU2109845C1 (en) Composition of concentrate for preparation of aqueous solution for deposition of coating, treatment of metal surfaces, aqueous solution for deposition of phosphate coating of crystalline structure to metal surface, method for phosphatization of metal surface and composition for replenishing of solution for deposition of coating
JP2680618B2 (en) Metal phosphate treatment method
US4824490A (en) Process of producing phosphate coatings on metals
JP2845246B2 (en) Method of forming phosphate film
KR20010072179A (en) Method for phosphatizing , rerinsing and cathodic electro-dipcoating
JP3137535B2 (en) Zinc-containing metal-coated steel sheet composite excellent in coatability and method for producing the same
US5268041A (en) Process for phosphating metal surfaces
CA1205726A (en) Phosphating solutions and process
JP2001508123A (en) How to phosphate a steel band
US3181976A (en) Phosphating process and composition
CA2247141A1 (en) Zinc phosphatising using low concentration of copper and mangnese
JPH07173643A (en) Method for phosphating metal surface and phosphating solution
CZ262398A3 (en) Metal surface phosphate coating process
US9309602B2 (en) Electrolytic iron metallizing of zinc surfaces
US6168674B1 (en) Process of phosphatizing metal surfaces
JPH0380877B2 (en)
JPH05331658A (en) Zinc phosphate treating method for metallic surface
JP2826242B2 (en) Phosphating of metal surfaces
JPH0149789B2 (en)
JP2001295063A (en) Method for forming phosphate film to nonferrous metallic material and plated steel sheet
JPH01240671A (en) Zinc phosphate treatment for metallic surface for coating
JPH0788585B2 (en) Phosphate film treatment agent

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080512

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090512

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100512

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110512

Year of fee payment: 11

EXPY Cancellation because of completion of term