EP0401616A1 - Process for applying manganese containing phosphate coatings on metallic surfaces - Google Patents

Process for applying manganese containing phosphate coatings on metallic surfaces Download PDF

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Publication number
EP0401616A1
EP0401616A1 EP90109944A EP90109944A EP0401616A1 EP 0401616 A1 EP0401616 A1 EP 0401616A1 EP 90109944 A EP90109944 A EP 90109944A EP 90109944 A EP90109944 A EP 90109944A EP 0401616 A1 EP0401616 A1 EP 0401616A1
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Prior art keywords
steel
aluminum
phosphate
phosphate coatings
manganese
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EP90109944A
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German (de)
French (fr)
Inventor
Matthias Hamacher
Jörg Riesop
Karl-Heinz Gottwald
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Henkel AG and Co KGaA
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Henkel AG and Co KGaA
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Publication of EP0401616A1 publication Critical patent/EP0401616A1/en
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    • 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
    • C23C22/364Chemical 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 also manganese cations
    • C23C22/365Chemical 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 also manganese cations containing also zinc and nickel 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

Definitions

  • the present invention relates to a method for producing manganese-containing phosphate coatings on surfaces made of steel, galvanized steel, aluminum and / or their alloys by spraying or dipping.
  • Aluminum can also be phosphated in combination with steel and galvanized steel to form a layer, whereby the generally achieved quality standard is guaranteed.
  • Composite parts of this type which consist of a wide variety of materials, for example aluminum and steel, have recently been used to an increasing extent in automobile construction.
  • EP-A 0 261 704 a method for producing phosphate coatings on such surfaces is known, wherein by spraying or spray-dipping to form uniform phosphate layers with a high degree of coverage, a phosphating solution is used which, in addition to zinc and phosphate, has at least one accelerator and one which must be precisely observed Must have the amount of fluoride ions. Furthermore, according to EP-A 0 261 704, the free acid content (FS) is to be adjusted according to a formula mentioned there.
  • the above object has been achieved by a process for producing manganese-containing phosphate coatings on surfaces made of steel, galvanized steel, aluminum and / or their alloys or aluminum-steel composites by spraying or spray-dipping with an aqueous solution 0.8 to 1.4 g / l Zn2+, 0.6 to 2.0 g / l Mn2+, 0.3 to 1.4 g / l Ni2+, 10 to 25 g / l PO43 ⁇ , 2 to 10 g / l NO3 ⁇ , 0.2 to 1.0 g / l F ⁇ and as an accelerator of phosphate separation 0.04 to 0.12 g / l NO2 ⁇ , 0.6 to 2.0 g / l ClO3 ⁇ and / or 0.2 to 1.0 g / l sodium 3-nitrobenzenesulfonate, the free acid content being adjusted to 1.4 to 1.8 points and having a total acid content of 18 to 30.
  • the free acid content in conventional low zinc processes is approximately 0.6 to 0.9 points. If the values are also increased, uneven, unclosed phosphate layers form on the metal surfaces treated in this way; The formation of flash rust is also observed on steel. In principle, the addition of manganese in the fluoride-containing phosphating baths makes it possible to increase the free acid content without the disadvantages mentioned.
  • the use of manganese in the phosphate layer has various advantages for the above-mentioned substrate surfaces.
  • the proven low-zinc technology can be retained to form phosphophyllite or manganese-containing phosphophyllite, and at the same time the zinc content can be increased without loss of quality.
  • the aluminum materials to be treated by the method according to the invention include the pure metal and its alloys. Pure aluminum, AlMg and AlMgSi kneading materials should therefore be mentioned as examples. A detailed description of these materials can be found in the aluminum paperback, 14th edition, Aluminum-Verlag, Düsseldorf, 1983.
  • the steels to be treated with the aid of the method according to the invention are, in particular, consumer goods such as automobile bodies, automobile accessories and spare parts, agricultural equipment, refrigerators and other types of small parts which are usually used in the form of sheet metal.
  • the term "galvanized steel” encompasses galvanizing by electrodeposition and hot dip application and thus refers to zinc and known zinc alloys.
  • the spraying time must be designed in such a way that a largely closed phosphate layer is formed.
  • full immersion systems are characterized by a large number of steps connected in series.
  • the term "full immersion system" results from the phosphating by immersion application.
  • spraying processes are also carried out, with spraying out of the immersion bath after the body has emerged.
  • a separate activation step is important for optimal phosphating.
  • pre-clean and activate the layer to be phosphated it is usually cleaned, rinsed and then activated in several work steps before phosphating.
  • aqueous suspensions containing titanium phosphate can be used here.
  • Compliance with the concentration ranges according to the main claim is an essential component for the production of high quality, i.e. uniform phosphate coatings. If the concentrations are undershot, the layers become uneven. In particular, their suitability for subsequent electrodeposition painting is decreasing.
  • the fluoride concentrations mentioned according to the invention are measured with a special ion-sensitive electrode in a buffered solution at pH 5.3. Therefore, these values are in no way comparable to the values mentioned in the prior art, in which the concentration of fluoride was measured directly in the phosphating solution.
  • the process is characterized by the use of an aqueous solution containing 0.8 to 1.0 g / l Zn2+, 0.8 to 1.2 g / l Mn2+, 0.3 to 0.8 g / l Ni2+, 14 to 20 g / l PO43 ⁇ , 3 to 6 g / l NO3 ⁇ and 0.3 to 0.6 g / l F ⁇ .
  • a further embodiment of the present invention consists in the application of the method for the preparation of the surfaces for electrocoating.
  • VDA test specification 621 4175 was used to investigate the corrosion resistance of the phosphating coatings mentioned below with various substrates. Following the coating, a standard electrophoresis dip coating (KET primer FT 85 7042 from BASF Maschinen und Lacke) was used.
  • the test time of the VDA alternating climate test is 5 to 10 rounds. During this time, the treated substrate is exposed to a condensation water change climate in accordance with DIN 50017 KFW. Furthermore, the substrate is stored for a certain time at room temperature (18 to 28 o C) according to DIN 50014 within the test period. Furthermore, a salt spray test in accordance with DIN 50021 is carried out as part of this alternating climate test.
  • a Phosphating solution containing manganese Substrate Infiltration at the cut 10 rounds 20 rounds Steel St 1405 0.6-0.8mm - Steel, electrolytically galvanized 2.0 - 2.5 mm - Aluminum (AlMg 0.4 Si 1.2) - 0.2 mm Aluminum "without fluoride - up to 10 mm B phosphating solution, manganese-free (comparison) Substrate Infiltration at the cut 10 rounds 20 rounds Steel St 1405 0.9 - 1.2 mm - Steel, electrolytically galvanized 3.4 - 4.0 mm - Aluminum (AlMg 0.4 Si 1.2) - 0.8 - 1.0 mm Aluminum "without fluoride - up to 10 mm

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  • 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)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

Process for producing manganese-containing phosphate coatings on metal surfaces, in particular steel, galvanized steel, aluminium and/or aluminium alloy or aluminium-steel composite surfaces, by spraying or spray dipping with an aqueous solution containing: 0,8 to 1,4 g/l of Zn<2+>, 0,6 to 2,0 g/l of Mn<2+>, 0,3 to 1,4 g/l of Ni<2+>, 10 to 25 g/l of PO4<3->, 2 to 10 g/l of NO3<->, 0,2 to 1,0 g/l of F<-> and as an accelerator for the phosphate precipitation 0,04 to 0,12 g/l of NO2<->, 0,6 to 2,0 g/l of ClO3<-> and/or 0,2 to 1,0 g/l of sodium-3-nitrobenzolsulphonate. The free acid content is adjusted to 1.4 to 1.8 and the solution has a total acid content of 18 to 30.

Description

Die vorliegende Erfindung betrifft ein Verfahren zur Erzeugung von manganhaltigen Phosphatüberzügen auf Oberflächen aus Stahl, ver­zinktem Stahl, Aluminium und/oder ihren Legierungen durch Spritzen oder Tauchen.The present invention relates to a method for producing manganese-containing phosphate coatings on surfaces made of steel, galvanized steel, aluminum and / or their alloys by spraying or dipping.

Zur Verbesserung des Korrosionsschutzes und der Lackhaftung werden Gebrauchsgüter wie Automobilkarossen, Automobilzubehör- und er­satzteile, landwirtschaftliche Geräte, Kühlschränke und jegliche Art von Kleinteilen nach sogenannten Niedrig-Zinkverfahren phos­phatiert und anschließend meist kataphoretisch tauchlackiert. Der­artige manganmodifizierte Zinkphosphatüberzüge als Haftgrund für moderne Lackieranlagen sind beispielsweise aus W.A. Roland und K.-H. Gottwald, Metalloberfläche, 1988/6 bekannt. Hier wird fest­gestellt, daß der Einsatz von Manganionen neben Zink- und Nickelionen in Niedrig-Zink-Phosphatierverfahren nachweislich den Korrosionsschutz verbessert, insbesondere bei Verwendung oberflächenveredelter Feinbleche. Der Einbau von Mangan in die Zinkphosphatüberzüge führt zu kleineren und kompakteren Kristallen mit höherer Alkalistabilität. Gleichzeitig wird die Arbeitsbreite von Phosphatierbädern erhöht; auch Aluminium kann im Verbund mit Stahl und verzinktem Stahl schichtbildend phosphatiert werden, wo­bei der allgemein erreichte Qualitätsstandard gewährleistet ist. Derartige Verbundwerkteile, die aus verschiedensten Materialien, beispielsweise aus Aluminium und Stahl bestehen, werden im Automo­bilbau in neuerer Zeit in erhöhtem Maße eingesetzt.In order to improve corrosion protection and paint adhesion, consumer goods such as automobile bodies, automotive accessories and spare parts, agricultural equipment, refrigerators and all kinds of small parts are phosphated using the so-called low-zinc process and then usually cataphoretically dip-coated. Such manganese-modified zinc phosphate coatings as a primer for modern painting systems are, for example, from WA Roland and K.-H. Gottwald, metal surface, 1988/6 known. It is found here that the use of manganese ions in addition to zinc and nickel ions in low-zinc phosphating processes has been shown to improve corrosion protection, in particular when surface-coated thin sheets are used. The incorporation of manganese into the zinc phosphate coatings leads to smaller and more compact crystals with higher alkali stability. At the same time, the working range of phosphating baths is increased; Aluminum can also be phosphated in combination with steel and galvanized steel to form a layer, whereby the generally achieved quality standard is guaranteed. Composite parts of this type, which consist of a wide variety of materials, for example aluminum and steel, have recently been used to an increasing extent in automobile construction.

Aus der EP-A 0 261 704 ist ein Verfahren zum Erzeugen von Phos­phatüberzügen auf derartigen Oberflächen bekannt, wobei durch Spritzen oder Spritztauchen zur Bildung gleichmäßiger Phosphat­schichten mit hohem Deckungsgrad mit einer Phosphatierungslösung gearbeitet wird, die neben Zink und Phosphat wenigstens einen Be­schleuniger sowie eine genau einzuhaltende Menge an Fluoridionen aufweisen muß. Weiterhin ist gemäß der EP-A 0 261 704 der Gehalt an freier Säure (FS) gemäß einer dort genannten Formel einzustel­len.From EP-A 0 261 704 a method for producing phosphate coatings on such surfaces is known, wherein by spraying or spray-dipping to form uniform phosphate layers with a high degree of coverage, a phosphating solution is used which, in addition to zinc and phosphate, has at least one accelerator and one which must be precisely observed Must have the amount of fluoride ions. Furthermore, according to EP-A 0 261 704, the free acid content (FS) is to be adjusted according to a formula mentioned there.

Demgegenüber ist Aufgabe der vorliegenden Erfindung, ein verbes­sertes Verfahren zur Erzeugung von Phosphatüberzügen auf Oberflä­chen aus Stahl, verzinktem Stahl, Aluminium und/oder ihren Legie­rungen bereitzustellen, das zu noch gleichmäßigeren Phosphatüber­zügen führt, wobei zudem eine Änderung der Phosphatierungstechnologie nicht erforderlich sein sollte.In contrast, it is an object of the present invention to provide an improved method for producing phosphate coatings on surfaces made of steel, galvanized steel, aluminum and / or their alloys, which leads to even more uniform phosphate coatings, and in addition, a change in the phosphating technology should not be necessary.

Die vorstehend genannte Aufgabe wurde gelöst durch ein Verfahren zum Erzeugen von manganhaltigen Phosphatüberzügen auf Oberflächen aus Stahl, verzinktem Stahl, Aluminium und/oder ihren Legierungen oder Aluminium-Stahl-Verbundwerkstoffen durch Spritzen oder Spritztauchen mit einer wäßrigen Lösung, enthaltend
0,8 bis 1,4 g/l Zn²⁺,
0,6 bis 2,0 g/l Mn²⁺,
0,3 bis 1,4 g/l Ni²⁺,
10 bis 25 g/l PO₄³⁻,
2 bis 10 g/l NO₃⁻,
0,2 bis 1,0 g/l F⁻ und
als Beschleuniger der Phosphatabscheidung
0,04 bis 0,12 g/l NO₂⁻,
0,6 bis 2,0 g/l ClO₃⁻ und/oder
0,2 bis 1,0 g/l Natrium-3-nitrobenzolsulfonat,
wobei der Gehalt an freier Säure auf 1,4 bis 1,8 Punkte eingestellt wird und einen Gesamtsäuregehalt von 18 bis 30 aufweist.
The above object has been achieved by a process for producing manganese-containing phosphate coatings on surfaces made of steel, galvanized steel, aluminum and / or their alloys or aluminum-steel composites by spraying or spray-dipping with an aqueous solution
0.8 to 1.4 g / l Zn²⁺,
0.6 to 2.0 g / l Mn²⁺,
0.3 to 1.4 g / l Ni²⁺,
10 to 25 g / l PO₄³⁻,
2 to 10 g / l NO₃⁻,
0.2 to 1.0 g / l F⁻ and
as an accelerator of phosphate separation
0.04 to 0.12 g / l NO₂⁻,
0.6 to 2.0 g / l ClO₃⁻ and / or
0.2 to 1.0 g / l sodium 3-nitrobenzenesulfonate,
the free acid content being adjusted to 1.4 to 1.8 points and having a total acid content of 18 to 30.

Bekanntermaßen beträgt bei üblichen Niedrigzink-Verfahren der Ge­halt an freier Säure etwa 0,6 bis 0,9 Punkte. Bei darüberhinaus erhöhten Werten bilden sich auf den so behandelten Metalloberflä­chen ungleichmäßige, nicht geschlossene Phosphatschichten; auf Stahl wird auch die Bildung von Flugrost beobachtet. Durch den Zu­satz von Mangan wird in den fluoridhaltigen Phosphatierungsbädern prinzipiell eine Erhöhung des Gehalts an freier Säure ohne die er­wähnten Nachteile möglich.As is known, the free acid content in conventional low zinc processes is approximately 0.6 to 0.9 points. If the values are also increased, uneven, unclosed phosphate layers form on the metal surfaces treated in this way; The formation of flash rust is also observed on steel. In principle, the addition of manganese in the fluoride-containing phosphating baths makes it possible to increase the free acid content without the disadvantages mentioned.

Die Verwendung von Mangen in der Phosphatschicht hat bei den oben genannten Substratoberflächen verschiedene Vorteile.The use of manganese in the phosphate layer has various advantages for the above-mentioned substrate surfaces.

Mit Hilfe der vorliegenden Erfindung wurde gefunden, daß insbeson­dere bei der Verwendung des erfindungsgemäßen Verfahrens auf Alu­miniumoberflächen eine relativ geringe Menge an Fluorid eingesetzt werden kann, um optisch gleichmäßige Phosphatschichten zu erzielen.With the help of the present invention, it was found that, in particular when using the method according to the invention, a relatively small amount of fluoride can be used on aluminum surfaces in order to achieve optically uniform phosphate layers.

Bei der Oberflächenbehandlung von Stahl kann zur Bildung von Phosphophyllit bzw. Mangan-haltigem Phosphophyllit die bewährte Niedrigzink-Technologie beibehalten werden und gleichzeitig der Zinkgehalt ohne Qualitätseinbuße erhöht werden.In the surface treatment of steel, the proven low-zinc technology can be retained to form phosphophyllite or manganese-containing phosphophyllite, and at the same time the zinc content can be increased without loss of quality.

Auf verzinkten, legierungsverzinkten Stahlblechen und auf Aluminium führt die Verwendung von Mangan bei gleichzeitig erhöhtem Zinkge­halt durch den Manganeinbau in die Schicht bei nachfolgender Beschichtung mittels kataphoretischer Elektrotauchlackierung zu verbesserten Ergebnissen. Diese gleichzeitige Wechselwirkung der Gehalte von Zink und Mangen in der Phosphatierungslösung wurde überraschenderweise mit Hilfe der vorliegenden Erfindung gefunden.On galvanized, alloy-galvanized steel sheets and on aluminum, the use of manganese with a simultaneously increased zinc content due to the manganese incorporation in the layer with subsequent coating by means of cataphoretic electrocoating leads to improved results. This simultaneous interaction of the Levels of zinc and manganese in the phosphating solution were surprisingly found using the present invention.

Die nach dem erfindungsgemäßen Verfahren zu behandelnden Alumini­um Werkstoffe umfassen das reine Metall und dessen Legierungen. Als Beispiele seien daher Reinaluminium-, AlMg- und AlMgSi- Knetwerkstoffe genannt. Eine ausführliche Darstellung dieser Werk­stoffe ist dem Aluminium-Taschenbuch, 14. Auflage, Aluminium-Ver­lag, Düsseldorf, 1983, zu entnehmen. Die mit Hilfe des erfindungsgemäßen Verfahrens zu behandelnden Stähle sind insbeson­dere Gebrauchsgüter wie Automobilkarossen, Automobilzubehör- und ersatzteile, landwirtschaftliche Geräte, Kühlschränke und sonstige Arten von Kleinteilen, die üblicherweise in Form von Blechen Ver­wendung finden. Der Begriff "verzinkter Stahl" umfaßt Verzinkungen durch elektrolytische Abscheidung und Schmelztauch-Applikation und bezieht sich somit auf Zink und bekannte Zinklegierungen.The aluminum materials to be treated by the method according to the invention include the pure metal and its alloys. Pure aluminum, AlMg and AlMgSi kneading materials should therefore be mentioned as examples. A detailed description of these materials can be found in the aluminum paperback, 14th edition, Aluminum-Verlag, Düsseldorf, 1983. The steels to be treated with the aid of the method according to the invention are, in particular, consumer goods such as automobile bodies, automobile accessories and spare parts, agricultural equipment, refrigerators and other types of small parts which are usually used in the form of sheet metal. The term "galvanized steel" encompasses galvanizing by electrodeposition and hot dip application and thus refers to zinc and known zinc alloys.

Bei der Durchführung des erfindungsgemäßen Verfahrens im Spritz-­Tauch-Modus muß die Spritzzeit derart gestaltet sein, daß eine weitgehend geschlossene Phosphatschicht ausgebildet wird.When the method according to the invention is carried out in spray-immersion mode, the spraying time must be designed in such a way that a largely closed phosphate layer is formed.

Moderne Volltauchanlagen zeichnen sich durch eine große Anzahl hintereinandergeschalteter Schritte aus. Der Begriff "Volltauchan­lage" resultiert aus der Phosphatierung durch Tauchapplikation. Bei anderen Verfahrensschritten werden auch Spritzvorgänge durchge­führt, wobei nach dem Auftauchen der Karosse aus dem Tauchbad nachgespritzt wird. Wichtig für eine optimale Phosphtierung ist ein separater Aktivierungsschritt. Zur Vorreinigung und Aktivierung der zu phosphatierenden Schicht wird diese üblicherweise in mehre­ren Arbeitsgängen gereinigt, gespült und anschließend vor dem Phosphatieren aktiviert. Beispielsweise können hier Titanphos­phat-haltige wäßrige Suspensionen eingesetzt werden.Modern full immersion systems are characterized by a large number of steps connected in series. The term "full immersion system" results from the phosphating by immersion application. In other process steps, spraying processes are also carried out, with spraying out of the immersion bath after the body has emerged. A separate activation step is important for optimal phosphating. To pre-clean and activate the layer to be phosphated, it is usually cleaned, rinsed and then activated in several work steps before phosphating. For example, aqueous suspensions containing titanium phosphate can be used here.

Die Einhaltung der Konzentrationsbereiche gemäß dem Hauptanspruch ist essentieller Bestandteil für die Erzeugung von qualitativ hochwertigen, d.h. gleichmäßigen Phosphatüberzügen. Bei Unterschreitung der Konzentrationen werden die Schichten ungleich­mäßig. Insbesondere nimmt ihre Eignung für die spätere Elektrotauchlackierung ab.Compliance with the concentration ranges according to the main claim is an essential component for the production of high quality, i.e. uniform phosphate coatings. If the concentrations are undershot, the layers become uneven. In particular, their suitability for subsequent electrodeposition painting is decreasing.

Die erfindungsgemäß genannten Fluoridkonzentrationen werden mit einer speziellen ionensensitiven Elektrode in gepufferter Lösung bei pH 5,3 gemessen. Daher sind diese Werte in keiner Weise ver­gleichbar mit den im Stand der Technik genannten Werten, in denen die Konzentration an Fluorid direkt in der Phosphatierungslösung gemessen wurde.The fluoride concentrations mentioned according to the invention are measured with a special ion-sensitive electrode in a buffered solution at pH 5.3. Therefore, these values are in no way comparable to the values mentioned in the prior art, in which the concentration of fluoride was measured directly in the phosphating solution.

In einer bevorzugten Ausführungsform der vorliegenden Erfindung ist das Verfahren gekennzeichnet durch den Einsatz einer wäßrigen Lö­sung, enthaltend 0,8 bis 1,0 g/l Zn²⁺,
0,8 bis 1,2 g/l Mn²⁺,
0,3 bis 0,8 g/l Ni²⁺,
14 bis 20 g/l PO₄³⁻,
3 bis 6 g/l NO₃⁻ und
0,3 bis 0,6 g/l F⁻.
In a preferred embodiment of the present invention, the process is characterized by the use of an aqueous solution containing 0.8 to 1.0 g / l Zn²⁺,
0.8 to 1.2 g / l Mn²⁺,
0.3 to 0.8 g / l Ni²⁺,
14 to 20 g / l PO₄³⁻,
3 to 6 g / l NO₃⁻ and
0.3 to 0.6 g / l F⁻.

Die mit Hilfe des obengenannten Verfahrens beschichteten Oberflä­chen können anschließend in bekannten Verfahren für die Elektrotauchlackierung eingesetzt werden. Demgemäß besteht eine weitere Ausführungsform der vorliegenden Erfindung in der Anwendung des Verfahrens zur Vorbereitung der Oberflächen für die Elektrotauchlackierung.The surfaces coated with the aid of the abovementioned process can then be used in known processes for electrocoating. Accordingly, a further embodiment of the present invention consists in the application of the method for the preparation of the surfaces for electrocoating.

Die Erfindung wird durch die folgenden Beispiele erläutert.The invention is illustrated by the following examples.

Beispiel 1:Example 1: Innerhalb der üblichen Prozeßfolge mit den Stufen:Within the usual process sequence with the stages:

Reinigen, Spülen, (Aktivieren) Phosphatieren, Spülen, Nachpassivieren,VE-Spülen, erfolgte die Konversionsbehandlung bei folgenden Badbedingungen entsprechend den drei Zusammensetzungen A, B und C: Applikationsart Badparameter Spritzen(A) Spritzen (Vergleich)(B) Spritz/Tauchen (C) "Freie Säure" (Punkte) 1,5 1,5 1,5 "Gesamtsäure" 26,5 26,3 22,2 Zn²⁺(g/l) 0,9 0,9 1,0 Mn²⁺(g/l) 0,9 - 0,6 Ni²⁺(g/l) 0,7 0,7 0,7 PO₄³⁻(g/l) 20,5 20,2 17,1 ClO₃⁻(g/l) 0,95 0,95 - F⁻(ppm)* 380 380 400 Beschleuniger** (ml Gas) Punkte 1,0 1,1 1,7 Temperatur (oC) 58 58 58 Zeit (s) 120 120 180 * gemessen mit einer ionensensitiven Elektrode in gepufferter Lösung bei pH 5,3 ** = Natriumnitrit - Für Stahl kann zur Bildung von Phosphophyllit bzw. manganhaltigem Phosphophyllit die "Niedrigzink"-Technologie beibehalten und der Zinkgehalt ohne Qualitätseinbuße angehoben werden.
- Auf verzinkten, legierungsverzinkten Stahlblechen und auf Alu­minium erfolgt durch den Manganeinbau in die Schicht bei nach­folgender Beschichtung mit einer KET-Grundierung eine deutliche Verbesserung der Korrosionsschutzergebnisse (siehe Beispiel 2).
Cleaning, rinsing, (activating) phosphating, rinsing, re-passivation, VE rinsing, the conversion treatment was carried out under the following bath conditions in accordance with the three compositions A, B and C: Application type Bath parameters Syringes (A) Syringes (comparison) (B) Spray / Dive (C) "Free Acid" (points) 1.5 1.5 1.5 "Total acidity" 26.5 26.3 22.2 Zn²⁺ (g / l) 0.9 0.9 1.0 Mn²⁺ (g / l) 0.9 - 0.6 Ni²⁺ (g / l) 0.7 0.7 0.7 PO₄³⁻ (g / l) 20.5 20.2 17.1 ClO₃⁻ (g / l) 0.95 0.95 - F⁻ (ppm) * 380 380 400 Accelerator ** (ml gas) points 1.0 1.1 1.7 Temperature ( o C) 58 58 58 Time (s) 120 120 180 * measured with an ion sensitive electrode in buffered solution at pH 5.3 ** = sodium nitrite - For steel, the "low zinc" technology can be retained to form phosphophyllite or manganese-containing phosphophyllite and the zinc content can be increased without loss of quality.
- On galvanized, alloy-galvanized steel sheets and on aluminum, the manganese incorporation in the layer with subsequent coating with a KET primer results in a significant improvement in the corrosion protection results (see example 2).

Die Bestimmung der flächenbezogenen Masse nach Anwendung der Ver­fahrensvariante A auf den einzelnen Substraten nach DIN 50942 ergab folgende Meßwerte (Mittelwerte): Stahl St 1405 2,0 g/m² Stahl, elektrolytisch verzinkt 2,4 g/m² Aluminium (AlMg 0,4 Si 1,2) 2,8 g/m² Aluminium (AlMg 4,5 Mn) 2,7 g/m² Durch Atomabsorptionsspektrometrie (AAS) wurde der Mangangehalt der Phosphatschicht quantitativ bestimmt (Mittelwerte): Stahl St 1405 6,4 % Stahl, elektrolytisch verzinkt 4,7 % Aluminium (AlMg 0,4 Si 1,2) 6,2 % Durch Röntgenbeugung werden bei den manganhaltigen Phosphatschich­ten keine neuen spezifischen Bande gefunden.The determination of the mass per unit area after application of process variant A on the individual substrates according to DIN 50942 resulted in the following measured values (mean values): Steel St 1405 2.0 g / m² Steel, electrolytically galvanized 2.4 g / m² Aluminum (AlMg 0.4 Si 1.2) 2.8 g / m² Aluminum (AlMg 4.5 Mn) 2.7 g / m² The manganese content of the phosphate layer was determined quantitatively by means of atomic absorption spectrometry (AAS): Steel St 1405 6.4% Steel, electrolytically galvanized 4.7% Aluminum (AlMg 0.4 Si 1.2) 6.2% No new specific band was found in the manganese-containing phosphate layers by X-ray diffraction.

Beispiel 2:Example 2:

Mit Hilfe des VDA-Wechselklimatests (VDA-Prüfvorschrift 621 415) wurde die Korrosionsbeständigkeit der nachfolgend genannten Phosphatierungsbeschichtungen mit verschiedenen Substraten unter­sucht. Im Anschluß an die Beschichtung wurde ein Standardelektro­phoresetauchlack (KET-Primer FT 85 7042 der BASF Farben und Lacke) eingesetzt.The VDA alternating climate test (VDA test specification 621 415) was used to investigate the corrosion resistance of the phosphating coatings mentioned below with various substrates. Following the coating, a standard electrophoresis dip coating (KET primer FT 85 7042 from BASF Farben und Lacke) was used.

Die Prüfzeit des VDA-Wechselklimatests beträgt 5 bis 10 Runden. Innerhalb dieser Zeit wird das behandelte Substrat entsprechend der DIN 50017 KFW einem Kondenswasser-Wechselklima ausgesetzt. Weiter­hin wird innerhalb des Prüfzeitraums das Substrat eine bestimmte Zeit bei Raumtemperatur (18 bis 28 oC) entsprechend DIN 50014 gelagert. Weiterhin wird im Rahmen dieses Wechselklimatests ein Salzsprühtest nach DIN 50021 durchgeführt.The test time of the VDA alternating climate test is 5 to 10 rounds. During this time, the treated substrate is exposed to a condensation water change climate in accordance with DIN 50017 KFW. Furthermore, the substrate is stored for a certain time at room temperature (18 to 28 o C) according to DIN 50014 within the test period. Furthermore, a salt spray test in accordance with DIN 50021 is carried out as part of this alternating climate test.

Nach Abschluß der Prüfzyklen wurden die nachfolgenden Daten ermit­telt. A Phosphatierungslösung, manganhaltig Substrat Unterwanderung am Schnitt 10 Runden 20 Runden Stahl St 1405 0,6 - 0,8 mm - Stahl, elektrolytisch verzinkt 2,0 - 2,5 mm - Aluminium (AlMg 0,4 Si 1,2) - 0,2 mm Aluminium " ohne Fluorid - bis 10 mm B Phosphatierungslösung, manganfrei (Vergleich) Substrat Unterwanderung am Schnitt 10 Runden 20 Runden Stahl St 1405 0,9 - 1,2 mm - Stahl, elektrolytisch verzinkt 3,4 - 4,0 mm - Aluminium (AlMg 0,4 Si 1,2) - 0,8 - 1,0 mm Aluminium " ohne Fluorid - bis 10 mm After the test cycles were completed, the following data were determined. A Phosphating solution, containing manganese Substrate Infiltration at the cut 10 rounds 20 rounds Steel St 1405 0.6-0.8mm - Steel, electrolytically galvanized 2.0 - 2.5 mm - Aluminum (AlMg 0.4 Si 1.2) - 0.2 mm Aluminum "without fluoride - up to 10 mm B phosphating solution, manganese-free (comparison) Substrate Infiltration at the cut 10 rounds 20 rounds Steel St 1405 0.9 - 1.2 mm - Steel, electrolytically galvanized 3.4 - 4.0 mm - Aluminum (AlMg 0.4 Si 1.2) - 0.8 - 1.0 mm Aluminum "without fluoride - up to 10 mm

Claims (4)

1. Verfahren zum Erzeugen von manganhaltigen Phosphatüberzügen auf Oberflächen aus Stahl, verzinktem Stahl, Aluminium und/oder ihren Legierungen oder Aluminium-Stahl-Verbundwerkstoffen durch Spritzen oder Spritztauchen mit einer wäßrigen Lösung, enthaltend
0,8 bis 1,4 g/l Zn²⁺,
0,6 bis 2,0 g/l Mn²⁺,
0,3 bis 1,4 g/l Ni²⁺,
10 bis 25 g/l PO₄³⁻,
2 bis 10 g/l NO₃⁻,
0,2 bis 1,0 g/l F⁻ und
als Beschleuniger der Phosphatabscheidung
0,04 bis 0,12 g/l NO₂⁻,
0,6 bis 2,0 g/l ClO₃⁻ und/oder
0,2 bis 1,0 g/l Natrium-3-nitrobenzolsulfonat,
wobei der Gehalt an freier Säure auf 1,4 bis 1,8 Punkte eingestellt wird und die Lösung einen Gesamtsäuregehalt von 18 bis 30 aufweist.
1. A method for producing manganese-containing phosphate coatings on surfaces made of steel, galvanized steel, aluminum and / or their alloys or aluminum-steel composites by spraying or spray-dipping with an aqueous solution containing
0.8 to 1.4 g / l Zn²⁺,
0.6 to 2.0 g / l Mn²⁺,
0.3 to 1.4 g / l Ni²⁺,
10 to 25 g / l PO₄³⁻,
2 to 10 g / l NO₃⁻,
0.2 to 1.0 g / l F⁻ and
as an accelerator of phosphate separation
0.04 to 0.12 g / l NO₂⁻,
0.6 to 2.0 g / l ClO₃⁻ and / or
0.2 to 1.0 g / l sodium 3-nitrobenzenesulfonate,
wherein the free acid content is adjusted to 1.4 to 1.8 points and the solution has a total acid content of 18 to 30.
2. Verfahren nach Anspruch, dadurch gekennzeichnet, daß man eine wäßrige Lösung, enthaltend
0,8 bis 1,0 g/l Zn²⁺,
0,8 bis 1,2 g/l Mn²⁺,
0,3 bis 0,8 g/l Ni²⁺,
14 bis 20 g/l PO₄³⁻,
3 bis 6 g/l NO₃⁻ und
0,3 bis 0,6 g/l F⁻
einsetzt.
2. The method according to claim, characterized in that one containing an aqueous solution
0.8 to 1.0 g / l Zn²⁺,
0.8 to 1.2 g / l Mn²⁺,
0.3 to 0.8 g / l Ni²⁺,
14 to 20 g / l PO₄³⁻,
3 to 6 g / l NO₃⁻ and
0.3 to 0.6 g / l F⁻
starts.
3. Verfahren nach Ansprüchen 1 bis 2, dadurch gekennzeichnet, daß die Phosphatüberzüge auf Aluminium-Stahl-Verbundwerkstoffen erzeugt werden.3. Process according to claims 1 to 2, characterized in that the phosphate coatings are produced on aluminum-steel composite materials. 4. Anwendung des Verfahrens nach Ansprüchen 1 bis 3 zur Vorberei­tung der Oberflächen für die Elektrotauchlackierung.4. Application of the method according to claims 1 to 3 for the preparation of the surfaces for electrocoating.
EP90109944A 1989-06-03 1990-05-25 Process for applying manganese containing phosphate coatings on metallic surfaces Withdrawn EP0401616A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3918136A DE3918136A1 (en) 1989-06-03 1989-06-03 METHOD FOR PRODUCING MANAGE-CONTAINING PHOSPHATE COATINGS ON METAL SURFACES
DE3918136 1989-06-03

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0659906A1 (en) * 1993-12-21 1995-06-28 Mazda Motor Corporation Method of phosphating metal surfaces and treatment solution
EP0759096A1 (en) * 1994-05-11 1997-02-26 Henkel Corporation A method for pre-treating aluminum materials prior to painting
EP0930379A1 (en) * 1998-01-14 1999-07-21 Nippon Paint Co., Ltd. Method of chemical conversion coating for low-lead electrodeposition coating
EP1012355A1 (en) * 1996-12-04 2000-06-28 Henkel Corporation Sludge reducing zinc phosphating process and composition

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Publication number Priority date Publication date Assignee Title
EP0135622A1 (en) * 1983-08-22 1985-04-03 Nippon Paint Co., Ltd. Phosphating metal surfaces
GB2148951A (en) * 1983-11-02 1985-06-05 Pyrene Chemical Services Ltd Phosphating processes and compositions
EP0228151A1 (en) * 1985-08-27 1987-07-08 HENKEL CORPORATION (a Delaware Corp.) Acidic, aqueous phosphate-coating solutions for use in a process for phosphate-coating metal surfaces
EP0261704A1 (en) * 1986-09-18 1988-03-30 Metallgesellschaft Ag Process for producing phosphate coatings on metal surfaces
EP0370535A1 (en) * 1988-11-25 1990-05-30 Metallgesellschaft Aktiengesellschaft Process for applying phosphate coatings

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JPS62174385A (en) * 1987-01-23 1987-07-31 Nippon Parkerizing Co Ltd Pretreatment for painting by cationic electrodeposition

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Publication number Priority date Publication date Assignee Title
EP0135622A1 (en) * 1983-08-22 1985-04-03 Nippon Paint Co., Ltd. Phosphating metal surfaces
GB2148951A (en) * 1983-11-02 1985-06-05 Pyrene Chemical Services Ltd Phosphating processes and compositions
EP0228151A1 (en) * 1985-08-27 1987-07-08 HENKEL CORPORATION (a Delaware Corp.) Acidic, aqueous phosphate-coating solutions for use in a process for phosphate-coating metal surfaces
EP0261704A1 (en) * 1986-09-18 1988-03-30 Metallgesellschaft Ag Process for producing phosphate coatings on metal surfaces
EP0370535A1 (en) * 1988-11-25 1990-05-30 Metallgesellschaft Aktiengesellschaft Process for applying phosphate coatings

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Title
PATENT ABSTRACTS OF JAPAN, Band 22, Heft 12 (C-470), 22. Januar 1988; & JP-A-62 174 385 (NIPPON PARKERIZING) 31-07-1987 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0659906A1 (en) * 1993-12-21 1995-06-28 Mazda Motor Corporation Method of phosphating metal surfaces and treatment solution
US5536336A (en) * 1993-12-21 1996-07-16 Nippon Paint Co., Ltd. Method of phosphating metal surfaces and treatment solution
EP0759096A1 (en) * 1994-05-11 1997-02-26 Henkel Corporation A method for pre-treating aluminum materials prior to painting
EP0759096A4 (en) * 1994-05-11 1997-06-04 Henkel Corp A method for pre-treating aluminum materials prior to painting
US5795407A (en) * 1994-05-11 1998-08-18 Henkel Corporation Method for pre-treating aluminum materials prior to painting
EP1012355A1 (en) * 1996-12-04 2000-06-28 Henkel Corporation Sludge reducing zinc phosphating process and composition
EP1012355A4 (en) * 1996-12-04 2000-06-28 Henkel Corp Sludge reducing zinc phosphating process and composition
EP0930379A1 (en) * 1998-01-14 1999-07-21 Nippon Paint Co., Ltd. Method of chemical conversion coating for low-lead electrodeposition coating

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EP0477204A1 (en) 1992-04-01
DE3918136A1 (en) 1990-12-06
JPH04505479A (en) 1992-09-24
KR920701517A (en) 1992-08-11
FI915683A0 (en) 1991-12-02
CA2058631A1 (en) 1990-12-04
ZA904222B (en) 1991-02-27
WO1990015167A1 (en) 1990-12-13
PT94242A (en) 1991-02-08

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