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EP1531012B1 - Supplementary corrosion protection for pieces of organic pre-coated metal sheets - Google Patents

Supplementary corrosion protection for pieces of organic pre-coated metal sheets Download PDF

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Publication number
EP1531012B1
EP1531012B1 EP04022644A EP04022644A EP1531012B1 EP 1531012 B1 EP1531012 B1 EP 1531012B1 EP 04022644 A EP04022644 A EP 04022644A EP 04022644 A EP04022644 A EP 04022644A EP 1531012 B1 EP1531012 B1 EP 1531012B1
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EP
European Patent Office
Prior art keywords
organic polymers
component
galvanized steel
coating based
metal
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
EP04022644A
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German (de)
French (fr)
Other versions
EP1531012A2 (en
EP1531012A3 (en
Inventor
Heike Quellhorst
Patrick Droniou
Alina Monica Koch
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Henkel AG and Co KGaA
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Henkel AG and Co KGaA
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Publication date
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Publication of EP1531012A2 publication Critical patent/EP1531012A2/en
Publication of EP1531012A3 publication Critical patent/EP1531012A3/en
Application granted granted Critical
Publication of EP1531012B1 publication Critical patent/EP1531012B1/en
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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/14Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/50Multilayers
    • B05D7/51One specific pretreatment, e.g. phosphatation, chromatation, in combination with one specific coating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/50Multilayers
    • B05D7/52Two layers
    • 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
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D2701/00Coatings being able to withstand changes in the shape of the substrate or to withstand welding

Definitions

  • the invention relates to a corrosion protection method for use in the production of painted metallic components from organically pre-coated metal sheets.
  • a corrosion protection layer which also serves as a primer for the subsequent painting.
  • a permanent corrosion-protective coating can be produced consisting of a conversion layer and a coating layer after assembly of the metallic components.
  • a well-known example of this is the process sequence phosphating and painting, as is common, for example, in the automotive industry.
  • the actual phosphating is only one step in a treatment sequence, which generally includes, in addition to cleaning and rinsing stages, activation before phosphating, the actual phosphating and often post-passivation after phosphating. Thereafter, join several paint on.
  • the pre-treatment before painting therefore requires several treatment steps, which in turn make a correspondingly extensive and thus costly pretreatment plant required.
  • heavy metal-containing waste which must be disposed of costly.
  • conversion layer is understood to mean a layer on a metal surface which is formed by “conversion treatment” under the action of a “conversion solution” and which both Contains elements of the metal surface as well as from the conversion solution.
  • conversion solution Typical examples are phosphate layers or chromate layers.
  • further conversion treatment methods are known, for example with conversion solutions based on complex fluorides of boron, silicon, titanium or zirconium. Most of these complex fluorides are used together with organic polymers. Examples of such conversion treatments are in DE-A-101 31 723 and the literature cited there. However, none of these alternative methods has been able to displace the phosphating pretreatment before painting in the automotive industry.
  • pre-coated metal strips are already offered on the market. On the one hand, these can be pre-phosphated, ie they can carry a phosphate layer but no further coating based on organic polymers. In the automotive and household appliance industry, metal strips are increasingly being processed which are already provided with a corrosion protection layer by the manufacturer of the strips.
  • Such materials are known, for example, under the names Granocoat R , Durasteel R , Bonazinc R and Durazinc R. They carry a thin organic coating over a conversion layer, for example a chromating or phosphating layer.
  • the organic coating consists of polymer systems such as epoxy or polyurethane resins, polyamides and polyacrylates. Solid additives such as silicic acids, zinc dust and soot improve the corrosion protection and, due to their electrical conductivity, allow the metal parts coated with layers of about 0.3 to about 10 ⁇ m, preferably up to about 5 ⁇ m, to be electrically welded and electrolytically painted.
  • the coating of the substrate materials is generally carried out in a two-stage process, in which first the inorganic conversion layer is produced and subsequently the organic polymer film is applied in a second treatment stage. More information can be found here DE-A-100 22 075 and the literature cited therein.
  • metal sheets provided in the band method with a coating based on organic polymers are already partially used in the construction of vehicle bodies, household appliances and furnishing articles.
  • the strictest requirements with regard to corrosion protection and adhesion of a subsequently applied Paints since vehicles are exposed to the strongest corrosion stresses.
  • no vehicle bodies are produced exclusively from organically pre-coated metal sheets. Rather, this material is possibly installed together with non-pre-coated sheets to the vehicle bodies.
  • the assembled bodies therefore currently undergo the usual pretreatment process before painting, ie they are subjected to the complex process sequence of phosphating.
  • the phosphating process could be replaced by a less expensive pretreatment process if the vehicle bodies were produced exclusively from organically precoated metal substrate.
  • the problem must be solved that inevitably arise in the assembly of bodies made of organically pre-coated metal sheets in places where the organic precoating is damaged or completely missing. This is the case, for example, at cut edges, at weld points and at cut points.
  • organically precoated metal substrates are frequently used in vehicle construction, in which serves as a metal substrate electrolytically galvanized or hot-dip galvanized steel.
  • the sites mentioned with a damaged organic layer are particularly difficult to treat, since they differ from the usual metal surfaces in terms of their electrochemical potentials and their chemical reactivity.
  • damaged areas are usually both shares of the steel substrate (ie iron) and the zinc coating bare.
  • a high local area ratio of steel (iron) to zinc may be present, for example a ratio of> 9: 1. This is particularly the case with cut edges, which represent a cross section through the coated steel substrate.
  • the corrosion conditions deviate from the other conditions on the homogeneous surface at these boundary areas, which combine zinc and iron. Depending on the local ratio of zinc to iron at the exposed metal sites, a different electrochemical potential arises between the potentials of zinc and iron. Furthermore, when machining the bodies grounded areas that have special conditions and thus special electrochemical potentials. Because the grinding process creates an activated interface of steel (iron) with finely divided reactive zinc.
  • the object of the invention is to provide, as part of a process for the production of painted metallic components which are composed of metal sheets pre-coated with organic polymers, a simpler method than phosphating which can be used to produce corrosion protection and lacquer adhesion at the damaged areas discussed
  • the present invention relates in a first aspect to a "claim 1".
  • All metal parts of the component should accordingly consist of organically pre-coated galvanized steel.
  • the component may still contain plastic components, as may be the case for example in the automotive industry.
  • the metallic components made of organically pre-coated galvanized steel can be assembled with plastic parts.
  • galvanized steel includes hot dip galvanized steels and electrolytically galvanized steels. Furthermore, alloy-galvanized steels are included, in which the coating For example, may consist of a zinc-nickel alloy or a zinc-aluminum alloy. The steels may be tempered to form an iron-zinc alloy at the interface between steel and zinc.
  • the joining of the sheets to the component in step a) can be carried out by the usual methods known in the art, for example by gluing, flanging, riveting, flanging and / or welding, in particular by arc welding.
  • joining by welding due to the associated damage to the coating based on organic polymers to more locations on the component arise that are not covered by the coating based on organic polymers.
  • passivated in sub-step c) as well as bare metal areas that result from grinding.
  • the process according to the invention is particularly suitable for the production of components with organically precoated metal sheets which have a coating based on organic polymers with a thickness in the range from 1 to 10 ⁇ m, the coating containing electrically conductive particles in addition to the organic polymers. Due to these characteristics of the organic coating, the components can be joined together by arc welding. Examples of such coatings are in DE-A-197 48 764 . DE-A-199 51 113 . DE-A-100 22 075 and in the literature cited therein. As mentioned in the introduction, metal strips with such coatings are commercially available under different trade names.
  • the passivation layer produced in sub-step c) should thus not represent a conventional zinc phosphate layer since, according to the present task, a process sequence which is shorter than that of zinc phosphating and thus more economical is to be used.
  • a zinc phosphate layer does not form if the treatment solution does not concurrently contain at least 0.3 g / l zinc ion and at least 3 g / l phosphate ion (as phosphoric acid or any protolysis step thereof).
  • the assembled component can be brought into contact in different ways with the acidic aqueous treatment solution, for example by immersion in the treatment solution or by spraying with the treatment solution. After this step you can rinse with water, but you do not have to. Ie. the method can be used as a "rinse” or "no-rinse” method.
  • the treatment according to sub-step c) does not represent a post-passivation of a preceding major conversion layer formation, but it is the only treatment step after the assembly of the components which produces a passivation layer on the bare metal sites.
  • the method sequence according to the invention can be used in the manufacture of vehicle bodies, household appliances, pieces of furniture, or in each case a part thereof.
  • the aqueous treatment solution in sub-step c) preferably has a pH of at least 2, in particular of at least 2.5, to at most 5, in particular to at most 4.
  • a pH of at least 2 in particular of at least 2.5, to at most 5, in particular to at most 4.
  • the pickling attack is increasingly too weak, so that only an insufficient passivation layer is formed.
  • the transitions in practice are fluent.
  • chromium-free acidic aqueous treatment solutions can be used, which are known in the art for the large-scale treatment of uncoated metal parts or metal strips.
  • a treatment solution is used, the total of at least 0.01 g / l, preferably at least 0.025 g / l, and up to 10 g / l, preferably up to 1 g / l, in particular to 0.5 g / l Ti- and or Zr and / or Si ions and at least one such amount of fluoride contains that the atomic ratio of Ti to F and / or Zr to F and / or Si to F in the range of 1: 1 to 1: 6, and which additionally contains at least 0.005 g / l, preferably at least 0.01 g / l, and up to 20 g / l, preferably up to 1 g / l of organic polymers.
  • the Ti, Zr and / or Si ions mentioned may be mentioned completely in the form of Hexafluorokomplexen such as the hexafluoroacids or their water in said concentration range salts such as the sodium salts. In this case, the atomic ratio is 1: 6.
  • complex compounds in which less than six fluoride ions in each case are connected to the central elements Ti, Zr or Si can form themselves in the treatment solution if hexafluoro complexes of at least one of the central elements Ti, Zr or Si and also at least one further compound of one of these central elements are added to it.
  • the treatment solution may be hexafluorozirconates and (preferably colloidal) silica (SiO 2 ) or their reaction products. Unreacted silica may be suspended in the treatment solution.
  • a treatment solution can also be obtained by using hydrofluoric acid or its (optionally acidic) salts together with those compounds of Ti, Zr and / or Si which can form fluorocomplexes herewith. Examples are the already mentioned nitrates, carbonates, hydroxides and / or oxides.
  • such an amount of Ti, Zr and / or Si is used as the central metal and such an amount of fluoride that the atomic ratio of central metal to fluoride is less than or equal to 1 to 2, in particular less than or equal to 1 to 3.
  • the atomic ratio may also become less than 1 to 6 when the treating solution contains more fluoride, for example in the form of hydrofluoric acid or its salts, than is stoichiometrically required to form the hexafluorocomplexes of the central metals Ti, Zr and / or Si.
  • the atomic ratio may become as small as 1 to 12 or 1:18, or even less, by employing a corresponding excess of fluoride, ie, two or three times or even more times what is necessary to complete formation of the hexafluoro complexes.
  • Suitable homopolymers or copolymers of vinylpyrrolidone are, for example, the polymers or polymers listed in Table 1 of the monomers mentioned there. Copolymers of vinylpyrrolidone with monomers having caprolactam or imidazole groups are particularly preferred.
  • the preferred treatment solutions described above preferably have a temperature in the range from 20 to 45 ° C, in particular from 30 to 40 ° C.
  • This treatment solution is preferably contacted with the cleaned assembled member for a period of time in the range of 1 to 5 minutes, more preferably 2 to 3 minutes.
  • the treatment solutions to be used should be free of chromium. It is further preferred that the acidic aqueous treatment solution except metals of the 4th subgroup of the periodic table (for example in the form of complex fluorides of Ti and / or Zr) contains no other subgroup metals ("transition metals"). As a result, the treatment of wastewater is simplified.
  • the metallic component pretreated in sub-step c), with or without intermediate rinsing as sub-step d), can be coated with a lacquer customary for the intended use.
  • a lacquer customary for the intended use For example, it may be selected from a dip paint, an electrodeposition paint or a powder paint.
  • the present invention relates to a painted component comprising galvanized steel metal parts obtainable by the method described above.
  • galvanized steel metal parts obtainable by the method described above.
  • this is understood to mean that all metal parts of the component consist of organically precoated galvanized steel.
  • the component may still contain plastic components, as may be the case for example in the automotive industry.
  • Example 1 Conversion treatment of molded parts (Material: Electrogalvanized with Granocoat ® ZE coating)
  • Gramocoat ® products are coating systems for galvanized steel on the basis of organic polymers and conductive pigments, as they are explained in detail in the foregoing description. These products are described in patent applications DE-A-100 22 075 (Granocoat ® ZE) and DE-A-100 22 075 Described (Granocoat ® S).)
  • Comparative Example 1 zinc phosphating of molded parts (material: Electrolytically galvanized with Granocoat ® coating ZE)
  • Example 2 Conversion treatment of molded parts (material: electrolytically galvanized with Granocoat ® S coating)
  • Example 3 Conversion treatment of molded parts (Material: Hot dip galvanized steel with Granocoat ® ZE coating)
  • Comparative Example 3 zinc phosphating of molded parts (material: fire galvanized steel with Granocoat ® coating ZE)
  • test results show that with the shorter process sequence according to the invention at least the same results as with a zinc phosphating.
  • the results according to the method of the invention tend to be even better than those achieved with zinc phosphating.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
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  • Application Of Or Painting With Fluid Materials (AREA)
  • Chemical Treatment Of Metals (AREA)
  • Laminated Bodies (AREA)

Abstract

The method is for the manufacture of a lacquered component containing metal parts of galvanized steel. All the metal parts during the carrying out of the manufacturing stages consist exclusively of sheets of galvanized steel which bear a coating on a base of organic polymers, whereby in a treatment stage a passivating layer is created on the sections of the metal surface which are not covered by the coating on the base of organic polymers. The metal component may be the body of a motor vehicle, a domestic appliance, or a piece of furniture. An independent claim is included for a lacquered component containing parts of galvanized steel produced by the aforesaid method.

Description

Die Erfindung betrifft ein Korrosionsschutzverfahren zur Anwendung bei der Herstellung von lackierten metallischen Bauteilen aus organisch vorbeschichteten Metallblechen. Hierbei werden Stellen aus unbeschichtetem Metall, die beim Schneiden, Umformen und Zusammenfügen der vorbeschichteten Metallbleche zwangsläufig entstehen, mit einer Korrosionsschutzschicht versehen, die gleichzeitig als Haftgrund für die nachfolgende Lackierung dient.The invention relates to a corrosion protection method for use in the production of painted metallic components from organically pre-coated metal sheets. In this case, places of uncoated metal, which inevitably arise during cutting, forming and joining the precoated metal sheets, provided with a corrosion protection layer, which also serves as a primer for the subsequent painting.

Aus Metallblechen zusammengefügte Bauteile wie beispielsweise Fahrzeugkarosserien, Gehäuse von Haushaltsgeräten oder metallische Möbelstücke können aus Metallblechen zusammengesetzt werden, die noch keine permanent korrosionsschützende Beschichtung aufweisen. In einer mehrere Stufen umfassenden Verfahrensfolge kann eine permanent korrosionsschützende Beschichtung bestehend aus einer Konversionsschicht und einer Lackierschicht nach dem Zusammenbau der metallischen Bauteile erzeugt werden. Ein bekanntes Beispiel hierfür ist die Verfahrensfolge Phosphatierung und Lackierung, wie sie beispielsweise im Automobilbau üblich ist. Dabei ist die eigentliche Phosphatierung nur ein Schritt in einer Behandlungsfolge, die in der Regel neben Reinigungs- und Spülstufen eine Aktivierung vor der Phosphatierung, die eigentliche Phosphatierung und häufig eine Nachpassivierung nach der Phosphatierung umfaßt. Danach schließen sich mehrere Lackierstufen an. Die Vorbehandlung vor der Lackierung erfordert also mehrere Behandlungsschritte, die wiederum eine entsprechend umfangreiche und damit kostenaufwendige Vorbehandlungsanlage erforderlich machen. Außerdem entstehen bei der Phosphatierung Schwermetall-haltige Abfälle, die kostenaufwendig entsorgt werden müssen.Components assembled from metal sheets such as vehicle bodies, housings of household appliances or metallic pieces of furniture can be assembled from metal sheets which do not yet have a permanent corrosion-protective coating. In a multi-stage process sequence, a permanent corrosion-protective coating can be produced consisting of a conversion layer and a coating layer after assembly of the metallic components. A well-known example of this is the process sequence phosphating and painting, as is common, for example, in the automotive industry. In this case, the actual phosphating is only one step in a treatment sequence, which generally includes, in addition to cleaning and rinsing stages, activation before phosphating, the actual phosphating and often post-passivation after phosphating. Thereafter, join several paint on. The pre-treatment before painting therefore requires several treatment steps, which in turn make a correspondingly extensive and thus costly pretreatment plant required. In addition, during phosphating heavy metal-containing waste, which must be disposed of costly.

Außer einer Phosphatierung sind weitere Verfahren zum Erzeugen einer sogenannten Konversionsschicht bekannt, die das darunter liegende Metall vor Korrosion schützt und die einen Haftgrund für eine nachfolgende Lackierschicht darstellt. Dabei wird unter einer "Konversionsschicht" eine Schicht auf einer Metalloberfläche verstanden, die durch "Konversionsbehandlung" unter Einwirkung einer "Konversionslösung" gebildet wird und die sowohl Elemente aus der Metalloberfläche als auch aus der Konversionslösung enthält. Typische Beispiele sind Phosphatschichten oder Chromatierschichten. Außer Phosphatier- und Chromatierverfahren sind weitere Verfahren zur Konversionsbehandlung bekannt, beispielsweise mit Konversionslösungen auf Basis komplexer Fluoride von Bor, Silicium, Titan oder Zirkon. Meistens werden diese komplexen Fluoride zusammen mit organischen Polymeren eingesetzt. Beispiele derartiger Konversionsbehandlungen sind in DE-A-101 31 723 und der dort zitierten Literatur genannt. Jedoch konnte keines dieser alternativen Verfahren bisher die Phosphatierung als Vorbehandlung vor der Lackierung im Automobilbau verdrängen.Apart from phosphating, other methods for producing a so-called conversion layer are known, which protect the underlying metal from corrosion and which constitutes a primer for a subsequent coating layer. Here, a "conversion layer" is understood to mean a layer on a metal surface which is formed by "conversion treatment" under the action of a "conversion solution" and which both Contains elements of the metal surface as well as from the conversion solution. Typical examples are phosphate layers or chromate layers. Apart from phosphating and chromating processes, further conversion treatment methods are known, for example with conversion solutions based on complex fluorides of boron, silicon, titanium or zirconium. Most of these complex fluorides are used together with organic polymers. Examples of such conversion treatments are in DE-A-101 31 723 and the literature cited there. However, none of these alternative methods has been able to displace the phosphating pretreatment before painting in the automotive industry.

Prinzipiell wäre es ökonomisch und ökologisch günstiger, metallische Bauteile aus bereits vom Hersteller der Metallbänder vorbeschichtetem Material herzustellen und nach dem Zusammenbau nur noch zu reinigen und zu lackieren. Mit der Vorbehandlung verbundener Abfall fiele dann zentralisiert bei den Herstellern der Metallbänder und nicht weit verstreut bei den Weiterverarbeitern der Metallbänder an. Dementsprechend werden vorbeschichtete Metallbänder bereits am Markt angeboten. Zum einen können diese vorphosphatiert sein, d. h. eine Phosphatschicht, aber keine weitere Beschichtung auf Basis organischer Polymere tragen. In der Automobil- und Haushaltsgeräteindustrie werden in zunehmendem Maße auch Metallbänder verarbeitet, die bereits beim Hersteller der Bänder mit einer Korrosionsschutzschicht versehen sind. Derartige Materialien sind beispielsweise unter dem Namen GranocoatR, DurasteelR, BonazincR und DurazincR bekannt. Sie tragen eine dünne organische Beschichtung über einer Konversionsschicht, beispielsweise einer Chromatier- oder Phosphatierschicht. Die organische Beschichtung besteht aus Polymersystemen wie beispielsweise Epoxy- oder Polyurethanharzen, Polyamiden und Polyacrylaten. Feste Additive wie Kieselsäuren, Zinkstaub und Ruß verbessern den Korrosionsschutz und erlauben es aufgrund ihrer elektrischen Leitfähigkeit, die mit Schichten einer Dicke von etwa 0,3 bis etwa 10 µm, vorzugsweise bis etwa 5 µm überzogenen Metallteile elektrisch zu schweißen und elektrolytisch zu lackieren. Die Beschichtung der Substratmaterialien erfolgt in der Regel in einem Zweistufenprozeß, bei dem zuerst die anorganische Konversionsschicht erzeugt und anschließend in einer zweiten Behandlungsstufe der organische Polymerfilm aufgebracht werden. Nähere Informationen hierzu können DE-A-100 22 075 und der darin zitierten Literatur entnommen werden.In principle, it would be economically and ecologically more favorable to produce metallic components from material already pre-coated by the manufacturer of the metal strips and only to clean and paint after assembly. Waste associated with the pretreatment would then be centralized by the manufacturers of the metal strips and not widely dispersed by the downstream converters of the metal strips. Accordingly, pre-coated metal strips are already offered on the market. On the one hand, these can be pre-phosphated, ie they can carry a phosphate layer but no further coating based on organic polymers. In the automotive and household appliance industry, metal strips are increasingly being processed which are already provided with a corrosion protection layer by the manufacturer of the strips. Such materials are known, for example, under the names Granocoat R , Durasteel R , Bonazinc R and Durazinc R. They carry a thin organic coating over a conversion layer, for example a chromating or phosphating layer. The organic coating consists of polymer systems such as epoxy or polyurethane resins, polyamides and polyacrylates. Solid additives such as silicic acids, zinc dust and soot improve the corrosion protection and, due to their electrical conductivity, allow the metal parts coated with layers of about 0.3 to about 10 μm, preferably up to about 5 μm, to be electrically welded and electrolytically painted. The coating of the substrate materials is generally carried out in a two-stage process, in which first the inorganic conversion layer is produced and subsequently the organic polymer film is applied in a second treatment stage. More information can be found here DE-A-100 22 075 and the literature cited therein.

Im Bandverfahren mit einer Beschichtung auf Basis organischer Polymere versehene Metallbleche werden also bereits teilweise beim Bau von Fahrzeugkarosserien, von Haushaltsgeräten und von Einrichtungsgegenständen eingesetzt. Dabei werden im Automobilbau die strengsten Anforderungen hinsichtlich Korrosionsschutz und Haftung eines nachträglich aufgebrachten Lacks gestellt, da Fahrzeuge den stärksten Korrosionsbeanspruchungen ausgesetzt sind. Derzeit werden noch keine Fahrzeugkarosserien ausschließlich aus organisch vorbeschichteten Metallblechen hergestellt. Vielmehr wird dieses Material allenfalls zusammen mit nicht vorbeschichteten Blechen zu den Fahrzeugkarosserien verbaut. Die zusammengebauten Karosserien durchlaufen daher derzeit noch das übliche Vorbehandlungsverfahren vor einer Lackierung, d. h. sie werden der aufwendigen Prozeßfolge der Phosphatierung unterzogen.Thus metal sheets provided in the band method with a coating based on organic polymers are already partially used in the construction of vehicle bodies, household appliances and furnishing articles. In the automotive industry, the strictest requirements with regard to corrosion protection and adhesion of a subsequently applied Paints, since vehicles are exposed to the strongest corrosion stresses. At present, no vehicle bodies are produced exclusively from organically pre-coated metal sheets. Rather, this material is possibly installed together with non-pre-coated sheets to the vehicle bodies. The assembled bodies therefore currently undergo the usual pretreatment process before painting, ie they are subjected to the complex process sequence of phosphating.

Prinzipiell könnte das Phosphatierverfahren durch ein weniger aufwendiges Vorbehandlungsverfahren ersetzt werden, wenn die Fahrzeugkarosserien ausschließlich aus organisch vorbeschichtetem Metallsubstrat hergestellt werden würden. Hierzu muß jedoch das Problem gelöst werden, daß beim Zusammenbau von Karosserien aus organisch vorbeschichteten Metallblechen zwangsläufig Stellen entstehen, an denen die organische Vorbeschichtung beschädigt ist oder ganz fehlt. Dies ist beispielsweise an Schnittkanten, an Schweißpunkten und an geschliffenen Stellen der Fall.In principle, the phosphating process could be replaced by a less expensive pretreatment process if the vehicle bodies were produced exclusively from organically precoated metal substrate. For this purpose, however, the problem must be solved that inevitably arise in the assembly of bodies made of organically pre-coated metal sheets in places where the organic precoating is damaged or completely missing. This is the case, for example, at cut edges, at weld points and at cut points.

Aus der Offenlegungsschrifit US 20031150524 entnimmt der Fachmann eine Lehre zur korrosionsschützenden Behandlung von aus lackierten Metallteilen von verzinktem Stahl zusammengesetzten Bauteilen, wobei Bereiche der Metalloberfläche des verzinkten Stahls vorliegen können, die nicht von einer Beschichtung auf Basis organischer Polymere bedeckt sind. Das zusammengesetzte Bauteil wird gemäß der US 2003/150524 mit einer chromfreien sauren wässrigen Zusammensetzung in Kontakt gebracht, die auf den freien Metalloberflächen des Bauteils eine Passivierungsschicht erzeugt, die keine kristalline Zinkphosphatschicht darstellt. Die US 2003/150524 beschränkt sich ausschließlich auf die korrosionsschützende Behandlung von Bauteilen, deren freie, unbeschichtete metallische Oberfläche zumindest zu 90% aus Nichteisenmetallen, insbesondere Zink, bestehen muss.From the Offenlegungsschrifit US 20031150524 One skilled in the art will deviate from doctrine for anticorrosive treatment of components composed of painted metal parts of galvanized steel, wherein there may be areas of the metal surface of the galvanized steel that are not covered by a coating based on organic polymers. The composite component is according to the US 2003/150524 contacted with a chromium-free acidic aqueous composition which produces on the free metal surfaces of the device a passivation layer which is not a crystalline zinc phosphate layer. The US 2003/150524 is restricted exclusively to the corrosion-protective treatment of components whose free, uncoated metallic surface must consist of at least 90% non-ferrous metals, in particular zinc.

Aus Gründen der besseren Korrosionsschutzwirkung werden im Fahrzeugbau häufig solche organisch vorbeschichteten Metallsubstrate eingesetzt, bei denen als Metallsubstrat elektrolytisch verzinkter oder schmelztauchverzinkter Stahl dient. Bei derartigen organisch beschichteten Metallsubstraten sind aber die genannten Stellen mit beschädigter organischer Schicht besonders schwierig zu behandeln, da sie sich hinsichtlich ihrer elektrochemischen Potentiale und ihrer chemischen Reaktivität von den üblichen Metalloberflächen unterscheiden. An solchen beschädigten Stellen liegen in der Regel sowohl Anteile des Stahlsubstrats (also Eisen) als auch der Zinkbeschichtung bloß. Dabei kann ein hohes lokales Flächenverhältnis von Stahl (Eisen) zu Zink vorliegen, beispielsweise ein Verhältnis von > 9 : 1. Insbesondere ist dies bei Schnittkanten der Fall, die einen Querschnitt durch das beschichtete Stahlsubstrat darstellen. Die Korrosionsverhältnisse weichen an diesen Grenzbereichen, die Zink und Eisen kombinieren, von den sonstigen Verhältnissen auf der homogenen Fläche ab. Je nach dem lokalen Verhältnis von Zink zu Eisen an den freiliegenden Metallstellen stellt sich ein unterschiedliches elektrochemisches Potential zwischen den Potentialen von Zink und Eisen ein. Weiterhin entstehen bei der Bearbeitung der Karosserien geschliffene Bereiche, die spezielle Verhältnisse und damit besondere elektrochemische Potentiale aufweisen. Denn durch den Schleifvorgang entsteht eine aktivierte Grenzfläche von Stahl (Eisen) mit fein verteiltem reaktiven Zink.For reasons of better corrosion protection, such organically precoated metal substrates are frequently used in vehicle construction, in which serves as a metal substrate electrolytically galvanized or hot-dip galvanized steel. In the case of such organically coated metal substrates, however, the sites mentioned with a damaged organic layer are particularly difficult to treat, since they differ from the usual metal surfaces in terms of their electrochemical potentials and their chemical reactivity. In such damaged areas are usually both shares of the steel substrate (ie iron) and the zinc coating bare. In this case, a high local area ratio of steel (iron) to zinc may be present, for example a ratio of> 9: 1. This is particularly the case with cut edges, which represent a cross section through the coated steel substrate. The corrosion conditions deviate from the other conditions on the homogeneous surface at these boundary areas, which combine zinc and iron. Depending on the local ratio of zinc to iron at the exposed metal sites, a different electrochemical potential arises between the potentials of zinc and iron. Furthermore, when machining the bodies grounded areas that have special conditions and thus special electrochemical potentials. Because the grinding process creates an activated interface of steel (iron) with finely divided reactive zinc.

Die Erfindung stellt sich die Aufgabe, im Rahmen eines Prozesses zur Herstellung lackierter metallischer Bauteile, die aus mit organischen Polymeren vorbeschichteten Metallblechen zusammengesetzt sind, ein einfacheres Verfahren als eine Phosphatierung zur Verfügung zu stellen, mit dem an den diskutierten Schadstellen Korrosionsschutz und Lackhaftung erzeugt werden kann, Die vorliegende Erfindung betrifft in einem ersten Aspekt ein "Anspruch 1".The object of the invention is to provide, as part of a process for the production of painted metallic components which are composed of metal sheets pre-coated with organic polymers, a simpler method than phosphating which can be used to produce corrosion protection and lacquer adhesion at the damaged areas discussed The present invention relates in a first aspect to a "claim 1".

Alle Metallteile des Bauteils sollen demnach aus organisch vorbeschichtetem verzinktem Stahl bestehen. Zusätzlich zu diesen Metallteilen kann das Bauteil jedoch noch Komponenten aus Kunststoff enthalten, wie es beispielsweise im Automobilbau der Fall sein kann. Zur Herstellung beispielsweise einer Fahrzeugkarossene können also die metallischen Bauteile aus organisch vorbeschichtetem verzinktem Stahl mit Kunststoffteilen zusammengefügt werden.All metal parts of the component should accordingly consist of organically pre-coated galvanized steel. In addition to these metal parts, however, the component may still contain plastic components, as may be the case for example in the automotive industry. For example, to produce a vehicle body, the metallic components made of organically pre-coated galvanized steel can be assembled with plastic parts.

Der Begriff "verzinkter Stahl" umfaßt im Schmelztauchverfahren verzinkte Stähle und elektrolytisch verzinkte Stähle. Weiterhin sind legierungsverzinkte Stähle umfaßt, bei denen die Beschichtung beispielsweise aus einer Zink-Nickel-Legierung oder einer Zink-Aluminium-Legierung bestehen kann. Die Stähle können nach getempert sein, so daß sich an der Grenzschicht zwischen Stahl und Zink eine Eiseh-Zink-Legierung bildet.The term "galvanized steel" includes hot dip galvanized steels and electrolytically galvanized steels. Furthermore, alloy-galvanized steels are included, in which the coating For example, may consist of a zinc-nickel alloy or a zinc-aluminum alloy. The steels may be tempered to form an iron-zinc alloy at the interface between steel and zinc.

Das Zusammenfügen der Bleche zu dem Bauteil im Teilschritt a) kann nach den üblichen im Stand der Technik bekannten Methoden erfolgen, beispielsweise durch Kleben, Flanschen, Nieten, Bördeln und/oder Schweißen, insbesondere durch Elektroschweißen. Neben dem Schneiden und/oder Stanzen im Teilschritt a) führt ein Fügen durch Schweißen aufgrund der hiermit verbundenen Beschädigung der Beschichtung auf Basis organischer Polymere dazu, daß weitere Stellen an dem Bauteil entstehen, die nicht von der Beschichtung auf Basis organischer Polymere bedeckt sind. Auch diese werden im Teilschritt c) passiviert, ebenso wie blanke Metallbereiche, die durch Abschleifen entstehen.The joining of the sheets to the component in step a) can be carried out by the usual methods known in the art, for example by gluing, flanging, riveting, flanging and / or welding, in particular by arc welding. In addition to the cutting and / or punching in sub-step a) joining by welding due to the associated damage to the coating based on organic polymers to more locations on the component arise that are not covered by the coating based on organic polymers. These are also passivated in sub-step c), as well as bare metal areas that result from grinding.

Das erfindungsgemäße Verfahren ist besonders zur Herstellung von Bauteilen mit organisch vorbeschichteten Blechen geeignet, die eine Beschichtung auf Basis organischer Polymere mit einer Dicke im Bereich von 1 bis 10 µm aufweisen, wobei die Beschichtung zusätzlich zu den organischen Polymeren elektrisch leitfähige Partikel enthält. Aufgrund dieser Merkmale der organischen Beschichtung können die Bauteile durch Elektroschweißen zusammengefügt werden. Beispiele derartiger Beschichtungen sind in DE-A-197 48 764 , DE-A-199 51 113 , DE-A-100 22 075 sowie in der darin jeweils zitierten Literatur enthalten. Wie einleitend erwähnt, sind Metallbänder mit derartigen Beschichtungen unter unterschiedlichen Handelsnamen kommerziell erhältlich.The process according to the invention is particularly suitable for the production of components with organically precoated metal sheets which have a coating based on organic polymers with a thickness in the range from 1 to 10 μm, the coating containing electrically conductive particles in addition to the organic polymers. Due to these characteristics of the organic coating, the components can be joined together by arc welding. Examples of such coatings are in DE-A-197 48 764 . DE-A-199 51 113 . DE-A-100 22 075 and in the literature cited therein. As mentioned in the introduction, metal strips with such coatings are commercially available under different trade names.

Die im Teilschritt c) erzeugte Passivierungsschicht soll also keine konventionelle Zinkphosphatschicht darstellen, da gemäß der vorliegenden Aufgabenstellung eine gegenüber einer Zinkphosphatierung verkürzte und damit wirtschaftlichere Verfahrensfolge verwendet werden soll. Eine Zinkphosphatschicht bildet sich nicht, wenn die Behandlungslösung nicht gleichzeitig mindestens 0,3 g/l Zinkionen und mindestens 3 g/l Phosphationen (als Phosphorsäure oder einer beliebigen Protolysestufe hiervon) enthält.The passivation layer produced in sub-step c) should thus not represent a conventional zinc phosphate layer since, according to the present task, a process sequence which is shorter than that of zinc phosphating and thus more economical is to be used. A zinc phosphate layer does not form if the treatment solution does not concurrently contain at least 0.3 g / l zinc ion and at least 3 g / l phosphate ion (as phosphoric acid or any protolysis step thereof).

Im Teilschritt c) kann man das zusammengefügte Bauteil auf unterschiedliche Weise mit der sauren wäßrigen Behandlungslösung in Kontakt bringen, beispielsweise durch Eintauchen in die Behandlungslösung oder durch Bespritzen mit der Behandlungslösung. Nach diesem Schritt kann mit Wasser gespült werden, muß aber nicht. D. h. das Verfahren kann als "rinse"- oder als "no-rinse"-Verfahren eingesetzt werden.In sub-step c), the assembled component can be brought into contact in different ways with the acidic aqueous treatment solution, for example by immersion in the treatment solution or by spraying with the treatment solution. After this step you can rinse with water, but you do not have to. Ie. the method can be used as a "rinse" or "no-rinse" method.

Dabei stellt die Behandlung gemäß Teilschritt c) keine Nachpassivierung einer vorausgehenden hauptsächlichen Konversionsschichtsbildung dar, sondern sie ist der einzige Behandlungsschritt nach dem Zusammenbau der Bauteile, der auf den blanken Metallstellen eine Passivierungsschicht erzeugt.In this case, the treatment according to sub-step c) does not represent a post-passivation of a preceding major conversion layer formation, but it is the only treatment step after the assembly of the components which produces a passivation layer on the bare metal sites.

Insbesondere kann die erfindungsgemäße Verfahrensfolge, bei der Herstellung von Fahrzeugkarosserien, Haushaltsgeräten, Möbelstücken, oder jeweils einem Teil hiervon eingesetzt werden.In particular, the method sequence according to the invention can be used in the manufacture of vehicle bodies, household appliances, pieces of furniture, or in each case a part thereof.

Die wäßrige Behandlungslösung im Teilschritt c) hat vorzugsweise einen pH-Wert von mindestens 2, insbesondere von mindestens 2,5, bis höchstens 5, insbesondere bis höchstens 4. Bei geringeren pH-Werten besteht zunehmend die Gefahr eines zu starken Beizangriffs und einer Beschädigung der Beschichtung auf Basis organischer Polymere. Bei pH-Werten oberhalb von 5 fällt der Beizangriff zunehmend zu schwach aus, so daß sich nur eine unzureichende Passivierungsschicht bildet. Selbstverständlich sind die Übergänge in der Praxis jeweils fließend.The aqueous treatment solution in sub-step c) preferably has a pH of at least 2, in particular of at least 2.5, to at most 5, in particular to at most 4. At lower pH values, there is an increasing danger of an excessive pickling attack and damage to the Coating based on organic polymers. At pH values above 5, the pickling attack is increasingly too weak, so that only an insufficient passivation layer is formed. Of course, the transitions in practice are fluent.

Im Teilschritt c) können chromfreie saure wäßrige Behandlungslösungen eingesetzt werden, die im Stand der Technik zur großflächigen Behandlung unbeschichteter Metallteile oder Metallbänder bekannt sind. Vorzugsweise wird eine Behandlungslösung eingesetzt, die insgesamt mindestens 0,01 g/l, vorzugsweise mindestens 0,025 g/l, und bis zu 10 g/l, vorzugsweise bis zu 1 g/l, insbesondere bis 0,5 g/l Ti- und/oder Zr- und/oder Si-lonen sowie mindestens eine solche Menge an Fluorid enthält, dass das Atomverhältnis Ti zu F und/oder Zr zu F und/oder Si zu F im Bereich von 1 : 1 bis 1 : 6 liegt, und die zusätzlich mindestens 0,005 g/l, vorzugsweise mindestens 0,01 g/l, und bis zu 20 g/l, vorzugsweise bis zu 1 g/l organische Polymere enthält Dabei können die genannten Ti-, Zr- und /oder Si-Ionen vollständig in Form von Hexafluorokomplexen wie beispielsweise den Hexafluorosäuren oder ihrer im genannten Konzentrationsbereich wasserlöslichen Salze wie beispielsweise der Natriumsalze eingesetzt werden. In diesem Fall beträgt das Atomverhältnis 1 : 6. Es können jedoch auch Komplexverbindungen eingesetzt werden, bei denen jeweils weniger als sechs Fluoridionen mit den Zentralelementen Ti, Zr oder Si verbunden sind. Diese können sich in der Behandlungslösung von selbst bilden, wenn zu dieser sowohl Hexafluorokomplexe mindestens eines der Zentralelemente Ti, Zr oder Si als auch mindestens eine weitere Verbindung eines dieser Zentralelemente zugegeben werden. Als solche weitere Verbindungen kommen beispielsweise Nitrate, Carbonate, Hydroxide und/oder Oxide desselben oder eines anderen der drei genannten Zentralelemente in Betracht. Beispielsweise kann die Behandlungslösung Hexafluorozirkonationen sowie (vorzugsweise kolloiden) Kieselsäure (SiO2) oder deren Reaktionsprodukte enthalten. Nicht umgesetzte Kieselsäure kann in der Behandlungslösung suspendiert sein. Eine derartige Behandlungslösung lässt sich auch dadurch erhalten, dass man Flusssäure oder deren (gegebenenfalls saure) Salze zusammen mit solchen Verbindungen von Ti, Zr und/oder Si einsetzt, die hiermit Fluorokomplexe bilden können. Beispiele sind die bereits genannten Nitrate, Carbonate, Hydroxide und/oder Oxide. Vorzugsweise setzt man insgesamt eine solche Menge an Ti, Zr und/oder Si als Zentralmetall und eine solche Menge an Fluorid ein, dass das Atomverhältnis Zentralmetall zu Fluorid kleiner oder gleich 1 zu 2, insbesondere kleiner oder gleich 1 zu 3 ist. Das Atomverhältnis kann auch kleiner als 1 zu 6 werden, wenn die Behandlungslösung mehr Fluorid, beispielsweise in Form von Flusssäure oder deren Salze enthält, als stöchiometrisch zur Bildung der Hexafluorokomplexe der Zentralmetalle Ti, Zr und/oder Si erforderlich ist. Beispielsweise kann das Atomverhältnis so klein werden wie 1 zu 12 oder 1 : 18 oder noch darunter, wenn man einen entsprechenden Überschuss an Fluorid einsetzt, d.h. die zwei- oder dreifache oder noch mehrfache Menge dessen, was zur vollständigen Bildung der Hexafluorokomplexe erforderlich ist.In step c) chromium-free acidic aqueous treatment solutions can be used, which are known in the art for the large-scale treatment of uncoated metal parts or metal strips. Preferably, a treatment solution is used, the total of at least 0.01 g / l, preferably at least 0.025 g / l, and up to 10 g / l, preferably up to 1 g / l, in particular to 0.5 g / l Ti- and or Zr and / or Si ions and at least one such amount of fluoride contains that the atomic ratio of Ti to F and / or Zr to F and / or Si to F in the range of 1: 1 to 1: 6, and which additionally contains at least 0.005 g / l, preferably at least 0.01 g / l, and up to 20 g / l, preferably up to 1 g / l of organic polymers. The Ti, Zr and / or Si ions mentioned may be mentioned completely in the form of Hexafluorokomplexen such as the hexafluoroacids or their water in said concentration range salts such as the sodium salts. In this case, the atomic ratio is 1: 6. However, it is also possible to use complex compounds in which less than six fluoride ions in each case are connected to the central elements Ti, Zr or Si. These can form themselves in the treatment solution if hexafluoro complexes of at least one of the central elements Ti, Zr or Si and also at least one further compound of one of these central elements are added to it. As such further compounds are, for example, nitrates, carbonates, hydroxides and / or oxides thereof or another of the three mentioned central elements into consideration. For example, the treatment solution may be hexafluorozirconates and (preferably colloidal) silica (SiO 2 ) or their reaction products. Unreacted silica may be suspended in the treatment solution. Such a treatment solution can also be obtained by using hydrofluoric acid or its (optionally acidic) salts together with those compounds of Ti, Zr and / or Si which can form fluorocomplexes herewith. Examples are the already mentioned nitrates, carbonates, hydroxides and / or oxides. Preferably, such an amount of Ti, Zr and / or Si is used as the central metal and such an amount of fluoride that the atomic ratio of central metal to fluoride is less than or equal to 1 to 2, in particular less than or equal to 1 to 3. The atomic ratio may also become less than 1 to 6 when the treating solution contains more fluoride, for example in the form of hydrofluoric acid or its salts, than is stoichiometrically required to form the hexafluorocomplexes of the central metals Ti, Zr and / or Si. For example, the atomic ratio may become as small as 1 to 12 or 1:18, or even less, by employing a corresponding excess of fluoride, ie, two or three times or even more times what is necessary to complete formation of the hexafluoro complexes.

Dabei können Behandlungslösungen eingesetzt werden, die im Stand der Technik bekannte Kombinationen von Inhaltsstoffen enthalten, beispielsweise gemäß US-A-5 129 967 eine Behandlunglösung, die in Wasser mindestens folgende Komponenten enthält:

  1. a) Polyacrylsaüre oder deren Homopolymere,
  2. b) Hexafluorozirkonsäure,
  3. c) 0,17 bis 0,3 g/l Fluorwasserstoffsäure und
  4. d) bis zu 0,6 g/l Hexafluorotitansäure,
gemäß EP-B-8 942 eine Behandlungslösung, enthaltend
  1. a) Polyacrylsäure oder eines Esters davon und
  2. b) mindestens einer der Verbindungen H2ZrF6, H2TiF6 und H2SiF6, wobei der pH-Wert der Lösung unterhalb von 3,5 liegt,
    (weitere Polymere, die in ähnlichen Behandlungsbädern eingesetzt werden können, sind in WO 02/20652 aufgeführt),
gemäß US-A-4 992 116 eine Behandlungslösung mit pH-Werten zwischen etwa 2,5 und 5, die mindestens drei Komponenten enthält:
  1. a) Phosphationen im Konzentrationsbereich zwischen 1,1x10-5 bis 5,3x10-3 mol/l, entsprechend 1 bis 500 mg/l,
  2. b) mindestens eine Fluorosäure eines Elements der Gruppe Zr, Ti, und Si und
  3. c) eine Polyphenolverbindung, erhältlich durch Umsetzung von Poly(vinylphenol) mit Aldehyden und organischen Aminen,
gemäß WO 92/07973 eine Behandlungslösung, die als wesentliche Komponenten in saurer wäßriger Lösung H2ZrF6 und ein 3-(N-C1-4alkyl-N-2-hydroxyethylaminomethyl)-4-hydroxystyrol-Polymer enthält.In this case, treatment solutions can be used which contain known combinations of ingredients in the prior art, for example according to US-A-5 129 967 a treatment solution containing at least the following components in water:
  1. a) polyacrylic acid or its homopolymers,
  2. b) hexafluorozirconic acid,
  3. c) 0.17 to 0.3 g / l hydrofluoric acid and
  4. d) up to 0.6 g / l hexafluorotitanic acid,
according to EP-B-8 942 a treatment solution containing
  1. a) polyacrylic acid or an ester thereof and
  2. b) at least one of the compounds H 2 ZrF 6 , H 2 TiF 6 and H 2 SiF 6 , the pH of the solution being below 3.5,
    (Further polymers which can be used in similar treatment baths are in WO 02/20652 listed)
according to US-A-4 992 116 a treatment solution with pH values between about 2.5 and 5, containing at least three components:
  1. a) phosphate ions in the concentration range between 1.1 × 10 -5 to 5.3 × 10 -3 mol / l, corresponding to 1 to 500 mg / l,
  2. b) at least one fluoro acid of an element of the group Zr, Ti, and Si and
  3. c) a polyphenol compound obtainable by reacting poly (vinylphenol) with aldehydes and organic amines,
according to WO 92/07973 a treating solution containing as essential components in acidic aqueous solution H 2 ZrF 6 and a 3- (NC 1-4 alkyl-N-2-hydroxyethylaminomethyl) -4-hydroxystyrene polymer.

Bevorzugt sind jedoch solche Behandlungslösungen, bei denen die organischen Polymere ausgewählt sind aus Homo- und Copolymeren von Vinylpyrrolidon. Derartige Behandlungslösungen sind beschrieben in DE-A-100 05 113 und DE-A-101 31 723 . Sofern demgemäß im erfindungsgemäßen Verfahren eine Behandlungslösung eingesetzt wird, die Copolymere von Vinylpyrrolidon enthält, können diese Copolymere außer Vinylpyrrolidon eines oder mehrere andere Monomere enthalten. Sie können also beispielsweise als Copolymere aus 2 Komponenten oder als Copolymere aus 3 Komponenten (= Terpolymere) vorliegen. Weiterhin können Mischungen von Homo- und zweikomponentigen Copolymeren, Homo- und Terpolymeren oder zweikomponentigen Copolymeren und Terpolymeren eingesetzt werden.However, preferred are those treatment solutions in which the organic polymers are selected from homopolymers and copolymers of vinylpyrrolidone. Such treatment solutions are described in DE-A-100 05 113 and DE-A-101 31 723 , If, accordingly, a treatment solution containing copolymers of vinylpyrrolidone is used in the process according to the invention, these copolymers can contain one or more other monomers besides vinylpyrrolidone. They may therefore be present, for example, as copolymers of 2 components or as copolymers of 3 components (= terpolymers). Furthermore, mixtures of homo- and two-component copolymers, homopolymers and terpolymers or two-component copolymers and terpolymers can be used.

Als Homo- oder Copolymere von Vinylpyrrolidon kommen beispielsweise die in Tabelle 1 aufgelisteten Polymere bzw. Polymere der dort angeführten Monomere in Betracht. Copolymere von Vinylpyrrolidon mit Monomeren, die Caprolactam- oder Imidazol-Gruppen aufweisen, sind besonders bevorzugt. Tabelle 1: Beispiele für Homo- oder Copolymere von Vinylpyrolidon Bezeichnung Handelsname bzw. Hersteller Vinylpyrrolidon, Homopolymer LuviskolR, BASF / ISP Vinylpyrrolidon/Vinylacetat LuviskolR, BASF / ISP Vinylpyrrolidon/Vinylcaprolactam LuvitecR, BASF VinylpyrrolidonNinylimidazol LuvitecR, BASF Vinylpyrrolidon/Vinylimidazoliummethylsulfat Luvitec, BASF Vinylpyrrolidon/Na-methacrylat LuviteCR, BASF Vinylpyrrolidon/Olefine ISPR, Antaron Vinylpyrrolidon/Dimethylaminoethylmethacrylat ISPR Vinylpyrrolidon/Dimethylaminopropylmethacrylamid ISPR, Styleze Vinylpyrrolidon/Dimethylaminoethylmethacrylat Ammoniumsalz ISPR, Gafquat VinylpyrrolidonNinylcaprolactam/Dimethylaminoethylmethacrylat ISPR Vinylpyrrolidon/Methacrylamidopropyltrimethylammonium-chlorid ISPR, Gafquat VinylpyrrolidonNinylcaprolactam/Dimethylaminoethylmethacrylat ISPR, Advantage Vinylpyrrolidon/Styrol ISPR, Antara Suitable homopolymers or copolymers of vinylpyrrolidone are, for example, the polymers or polymers listed in Table 1 of the monomers mentioned there. Copolymers of vinylpyrrolidone with monomers having caprolactam or imidazole groups are particularly preferred. <u> Table 1 </ u>: Examples of Homopolymers or Copolymers of Vinylpyrolidone description Trade name or manufacturer Vinyl pyrrolidone, homopolymer Luviskol R , BASF / ISP Vinylpyrrolidone / vinyl acetate Luviskol R , BASF / ISP Vinylpyrrolidone / vinyl caprolactam Luvitec R , BASF VinylpyrrolidonNinylimidazol Luvitec R , BASF Vinylpyrrolidone / vinylimidazolium Luvitec, BASF Vinylpyrrolidone / Na methacrylate Luvite C R , BASF Vinylpyrrolidone / olefins ISP R , Antaron Vinylpyrrolidone / dimethylaminoethyl ISP R Vinylpyrrolidone / dimethylaminopropylmethacrylamide ISP R , Styleze Vinyl pyrrolidone / dimethylaminoethyl methacrylate ammonium salt ISP R , Gafquat VinylpyrrolidonNinylcaprolactam / dimethylaminoethyl ISP R Vinylpyrrolidone / methacrylamidopropyltrimethylammonium chloride ISP R , Gafquat VinylpyrrolidonNinylcaprolactam / dimethylaminoethyl ISP R , Advantage Vinylpyrrolidone / styrene ISP R , Antara

Die vorstehend beschriebenen bevorzugten Behandlungslösungen weisen vorzugsweise eine Temperatur im Bereich von 20 bis 45 °C, insbesondere von 30 bis 40 °C auf. Diese Behandlungslösung bringt man vorzugsweise für eine Zeitdauer im Bereich von 1 bis 5 Minuten, insbesondere von 2 bis 3 Minuten mit dem gereinigten zusammengefügten Bauteil in Kontakt.The preferred treatment solutions described above preferably have a temperature in the range from 20 to 45 ° C, in particular from 30 to 40 ° C. This treatment solution is preferably contacted with the cleaned assembled member for a period of time in the range of 1 to 5 minutes, more preferably 2 to 3 minutes.

Die einzusetzenden Behandlungslösungen sollen definitionsgemäß frei von Chrom sein. Dabei ist es weiterhin bevorzugt, daß die saure wäßrige Behandlungslösung außer Metallen der 4. Nebengruppe des Periodensystems (beispielsweise in Form komplexer Fluoride von Ti und/oder Zr) keine anderen Nebengruppenmetalle ("Übergangsmetalle") enthält. Hierdurch wird die Behandlung anfallender Abwässer vereinfacht.By definition, the treatment solutions to be used should be free of chromium. It is further preferred that the acidic aqueous treatment solution except metals of the 4th subgroup of the periodic table (for example in the form of complex fluorides of Ti and / or Zr) contains no other subgroup metals ("transition metals"). As a result, the treatment of wastewater is simplified.

Im Teilschritt e) kann das im Teilschritt c) vorbehandelte metallische Bauteil - mit oder ohne Zwischenspülung als Teilschritt d) - mit einem für die vorgesehene Verwendung üblichen Lack beschichtet werden. Beispielsweise kann dieser ausgewählt sein aus einem Tauchlack, einem Elektrotauchlack oder einem Pulverlack.In sub-step e), the metallic component pretreated in sub-step c), with or without intermediate rinsing as sub-step d), can be coated with a lacquer customary for the intended use. For example, it may be selected from a dip paint, an electrodeposition paint or a powder paint.

In einem zweiten Aspekt betrifft die vorliegende Erfindung ein lackiertes, Metallteile aus verzinktem Stahl enthaltendes Bauteil, das nach dem vorstehend beschriebenen Verfahren erhältlich ist. Wie vorstehend erläutert, ist hierunter zu verstehen, daß alle Metallteile des Bauteils aus organisch vorbeschichtetem verzinktem Stahl bestehen. Zusätzlich zu diesen Metallteilen kann das Bauteil jedoch noch Komponenten aus Kunststoff enthalten, wie es beispielsweise im Automobilbau der Fall sein kann.In a second aspect, the present invention relates to a painted component comprising galvanized steel metal parts obtainable by the method described above. As explained above, this is understood to mean that all metal parts of the component consist of organically precoated galvanized steel. In addition to these metal parts, however, the component may still contain plastic components, as may be the case for example in the automotive industry.

Durch das erfindungsgemäße Verfahren lassen sich lackierte metallische Bauteile wie beispielsweise Fahrzeugkarosserien, Haushaltsgeräte, Möbel oder jeweils Teile hiervon erhalten, die alle derzeitigen Ansprüche an Aussehen, Korrosionsbeständigkeit und Lackhaftung erfüllen. Durch den ausschließlichen Einsatz von organisch vorbeschichtetem Rohmaterial kann beim Hersteller der Bauteile die erforderliche chemische Behandlung wesentlich verkürzt werden. Dies bringt für den Hersteller der Bauteile wirtschaftliche und ökologische Vorteile mit sich, da eine weniger aufwendige Vorbehandlungsanlage ausreicht und da weniger chemikalienbelastete Abwässer anfallen.By the method according to the invention can be obtained painted metallic components such as vehicle bodies, household appliances, furniture or in each case parts thereof, which meet all current requirements for appearance, corrosion resistance and paint adhesion. The exclusive use of organically pre-coated raw material can significantly shorten the required chemical treatment for the component manufacturer. This brings economic and environmental advantages for the manufacturer of the components, since a less expensive pretreatment plant is sufficient and there are less wastewater contaminated with chemicals.

Anwendungsbeispieleapplications Beispiel 1:Example 1: Konversionsbehandlung von geformten Teilen (Material: Elektrolytisch verzinkt mit Granocoat® ZE Beschichtung)Conversion treatment of molded parts (Material: Electrogalvanized with Granocoat ® ZE coating)

(Die in den Beispielen genannten "Granocoat®"-Produkte sind Beschichtungssysteme für verzinkten Stahl auf Basis von organischen Polymeren und Leitfähigkeitspigmenten, wie sie in der vorstehenden Beschreibung näher erläutert sind. Diese Produkte sind in den Patentanmeldungen DE-A-100 22 075 (Granocoat® ZE) und DE-A-100 22 075 (Granocoat® S) beschrieben.)(Referred to in the Examples, "Granocoat ®" products are coating systems for galvanized steel on the basis of organic polymers and conductive pigments, as they are explained in detail in the foregoing description. These products are described in patent applications DE-A-100 22 075 (Granocoat ® ZE) and DE-A-100 22 075 Described (Granocoat ® S).)

Prozessfolge (Tauchapplikation):Process sequence (immersion application):

1.1. Reinigung:Cleaning: Ridoline® 1570, 2 %; Ridosol® 1237, 0,3 %; 5 Minuten; 55 °CRidoline ® 1570 2%; Ridosol ® 1237, 0.3%; 5 minutes; 55 ° C 2.Second Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 3.Third Konversionsbehandlung:Conversion treatment: 180 Sekunden; 30°C; pH Wert 3.8; Badzusammensetzung:180 seconds; 30 ° C; pH 3.8; Bath composition: H2ZrF6-Säure (45 %ig; entsprechend 150 mg/l Zr) Luvitec® VPI 55 K18P (Fa. BASF, Ludwigshafen), ein Vinylpyrrolidon-Vinylimidazol-Copolymer (CAS-Nr. 172890-92-5), entsprechend einem Festkörpergehalt von 40 mg/l PolymerH 2 ZrF 6 acid (45%; corresponding to 150 mg / l Zr) Luvitec VPI 55 K18P ® (BASF, Ludwigshafen, Germany.), A vinylpyrrolidone-vinylimidazole copolymer according to (CAS No. 172890-92-5). a solids content of 40 mg / l polymer 4.4th Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 5.5th Trocknen:Dry: Pressluft, anschließend 50 °C 10 MinutenCompressed air, then 50 ° C for 10 minutes

Test: SAE J 2334 Test 80 RundenTest: SAE J 2334 test 80 rounds Vergleichsbeispiel 1: Zinkphosphatierung von geformten Teilen (Material: Elektrolytisch verzinkt mit Granocoat® ZE Beschichtung) Comparative Example 1: zinc phosphating of molded parts (material: Electrolytically galvanized with Granocoat ® coating ZE) Prozessfolge (Tauchapplikation):Process sequence (immersion application):

1.1. Reinigung:Cleaning: Ridoline® 1570, 2 %; Ridosol® 1237, 0,3 %; 5 Minuten; 55 °CRidoline ® 1570 2%; Ridosol ® 1237, 0.3%; 5 minutes; 55 ° C 2.Second Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 3.Third Aktivierung:Activation: gemäß Stand der Technikaccording to the prior art 4.4th Zinkphosphatierung:zinc phosphate: gemäß Stand der Technikaccording to the prior art 5.5th Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 6.6th Trocknen:Dry: Pressluft, anschließend 50 °C 10 MinutenCompressed air, then 50 ° C for 10 minutes

Test: SAE J 2334 Test 80 RundenTest: SAE J 2334 test 80 rounds Beispiel 2: Konversionsbehandlung von geformten Teilen (Material: Elektrolytisch verzinkt mit Granocoat® S Beschichtung) Example 2: Conversion treatment of molded parts (material: electrolytically galvanized with Granocoat ® S coating) Prozessfolge (Tauchapplikation):Process sequence (immersion application):

1.1. Reinigung:Cleaning: Ridoline® 1570, 2 %; Ridosol® 1237, 0,3 %; 5 Minuten; 55 °CRidoline ® 1570 2%; Ridosol ® 1237, 0.3%; 5 minutes; 55 ° C 2.Second Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 3.Third Konversionsbehandlung:Conversion treatment: 180 Sekunden; 30 °C; pH Wert 3,8; Badzusammensetzung:180 seconds; 30 ° C; pH 3.8; Bath composition: H2ZrF6-Säure (45 %ig; entsprechend 150 mg/l Zr)H 2 ZrF 6 acid (45%, corresponding to 150 mg / l Zr) Luvitec® VPI 55 K18P (Fa. BASF) entsprechend einem Festkörpergehalt von 40 mg/l PolymerLuvitec VPI 55 K18P ® (Fa. BASF) corresponding to a solids content of 40 mg / l Polymer 4.4th Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 5.5th Trocknen:Dry: Pressluft, anschließend 50 °C 10 MinutenCompressed air, then 50 ° C for 10 minutes

Test: SAE J 2334 Test 80 RundenTest: SAE J 2334 test 80 rounds Vergleichsbeispiel 2: Zinkphosphatierung von geformten Teilen (Material: Elektrolytisch verzinkt mit Granocoat® S Beschichtung) Comparative Example 2 Zinc phosphating of molded parts (material: Electrolytically galvanized with Granocoat ® S coating) Prozessfolge (Tauchapplikation):Process sequence (immersion application):

1.1. Reinigung:Cleaning: Ridoline® 1570, 2 %; Ridosol® 1237, 0,3 %; 5 Minuten; 55 °CRidoline ® 1570 2%; Ridosol ® 1237, 0.3%; 5 minutes; 55 ° C 2.Second Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 3.Third Aktivierung:Activation: gemäß Stand der Technikaccording to the prior art 4.4th Zinkphosphatierung:zinc phosphate: gemäß Stand der Technikaccording to the prior art 5.5th Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 6.6th Trocknen:Dry: Pressluft, anschließend 50 °C 10 MinutenCompressed air, then 50 ° C for 10 minutes

Test: SAE J 2334 Test 80 RundenTest: SAE J 2334 test 80 rounds Beispiel 3: Konversionsbehandlung von geformten Teilen (Material: Feuerverzinkter Stahl mit Granocoat® ZE Beschichtung) Example 3: Conversion treatment of molded parts (Material: Hot dip galvanized steel with Granocoat ® ZE coating) Prozessfolge (Tauchapplikation):Process sequence (immersion application):

1.1. Reinigung:Cleaning: Ridoline® 1570, 2 %; Ridosol® 1237, 0,3 %; 5 Minuten; 55 °CRidoline ® 1570 2%; Ridosol ® 1237, 0.3%; 5 minutes; 55 ° C 2.Second Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 3.Third Konversionsbehandlung:Conversion treatment: 180 Sekunden; 30 °C; pH Wert 3.8; Badzusammensetzung:180 seconds; 30 ° C; pH 3.8; Bath composition: H2ZrF6-Säure (45 %ig; entsprechend 150 mg/l Zr)H 2 ZrF 6 acid (45%, corresponding to 150 mg / l Zr) Luvitec® VPI 55 K18P (Fa. BASF) entsprechend einem Festkörpergehalt von 40 mg/l PolymerLuvitec VPI 55 K18P ® (Fa. BASF) corresponding to a solids content of 40 mg / l Polymer 4. Spüle:4. sink: vollentsalztes Wassercompletely desalinated water 5. Trocknen:5. Drying: Pressluft, anschließend 50 °C 10 MinutenCompressed air, then 50 ° C for 10 minutes

Test: SAE J 2334 Test 80 RundenTest: SAE J 2334 test 80 rounds Vergleichsbeispiel 3: Zinkphosphatierung von geformten Teilen (Material: Feuer verzinkter Stahl mit Granocoat® ZE Beschichtung) Comparative Example 3: zinc phosphating of molded parts (material: fire galvanized steel with Granocoat ® coating ZE) Prozessfolge (Tauchapplikation):Process sequence (immersion application):

1.1. Reinigung:Cleaning: Ridoline 1570, 2 %; Ridosol 1237, 0,3%; 5 Minuten; 55 °CRidoline 1570, 2%; Ridosol 1237, 0.3%; 5 minutes; 55 ° C 2.Second Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 3.Third Aktivierung:Activation: gemäß Stand der Technikaccording to the prior art 4.4th Zinkphosphatierung:zinc phosphate: gemäß Stand der Technikaccording to the prior art 5.5th Spüle:Kitchen sink: vollentsalztes Wassercompletely desalinated water 6.6th Trocknen:Dry: Pressluft, anschließend 50 °C 10 MinutenCompressed air, then 50 ° C for 10 minutes

Test: SAE J 2334 Test 80 RundenTest: SAE J 2334 test 80 rounds Ergebnisse der BeispieleResults of the examples

Beispiel 1example 1 Vergleichs-beispiel 1Comparative Example 1 Beispiel 2Example 2 Vergleichs-beispiel 2Comparative Example 2 Beispiel 3Example 3 Vergleichs-beispiel 3Comparative Example 3 Korrosion an KantenCorrosion on edges XX Korrosion im FlanschbereichCorrosion in the flange area XX Korrosion in umgeformter FlächeCorrosion in formed area XX XX XX ○ Keine Korrosionsprodukte vorhanden
□ wenige Punkte Korrosion vorhanden
X Rotrostprodukte vorhanden
○ No corrosion products present
□ few points of corrosion
X red rust products available

Die Testergebnisse zeigen, daß mit der erfindungsgemäßen, kürzeren Verfahrensfolge mindestens die selben Ergebnisse mit der werden wie mit einer Zinkphosphatierung. Tendenziell sind die Ergebnisse gemäß dem erfindungsgemäßen Verfahren sogar besser als diejenigen, die man mit einer Zinkphosphatierung erzielt.The test results show that with the shorter process sequence according to the invention at least the same results as with a zinc phosphating. The results according to the method of the invention tend to be even better than those achieved with zinc phosphating.

Claims (11)

  1. A method for manufacturing a lacquered component containing metal parts in galvanized steel, wherein
    a) sheets in galvanized steel, which bear a coating based on organic polymers, are cut and/or punched and/or deformed and the thereby obtained metal parts are assembled for manufacturing the component, regions of the metal surface of the galvanized steel being formed which are not covered by the coating based on organic polymers and which have a surface ratio of steel to zinc which is greater than 9:1;
    b) the assembled component is cleaned,
    c) the cleaned assembled component is brought into contact with an aqueous chromium-free acid treatment solution, which produces on the regions of the metal surface formed in partial step a), which are not covered by the coating based on organic polymers, a passivation layer which does not represent a zinc phosphate layer,
    d) if desired, but not mandatorily, the component treated in partial step c) is rinsed one or several times with water and
    e) is coated with a lacquer coating,
    wherein all the metal parts of the component during the execution of the partial steps b) to e) exclusively consist of the sheets in galvanized steel, which bear a coating based on organic polymers, and wherein the partial step c) is the only treatment step after the partial step a), which produces a passivation layer on the regions of the metal surface formed in partial step a), which are not covered by the coating based on organic polymers.
  2. The method according to claim 1, characterized in that as for the metal component, this is a vehicle body, a household appliance, a piece of furniture, or respectively a portion thereof.
  3. The method according to one or both of claims 1 and 2, characterized in that the coating based on organic polymers has a thickness in the range from 1 to 10 µm and in addition to the organic polymers, contains electrically conducting particles.
  4. The method according to one or more of claims 1 to 3, characterized in that the aqueous acid treatment solution in partial step c) has a pH value in the range from at least 2, preferably at least 2.5 to at most 5, preferably to at most 4.
  5. The method according to one or more of claims 1 to 4, characterized in that the aqueous acid treatment solution all in all contains at least 0.01 g/L, preferably at least 0.025 g/L, and up to 10 g/L, preferably up to 1 g/L, in particular up to 0.5 g/L of Ti and/or Zr and/or Si ions as well as at least an amount of fluoride such that the atomic ratio of Ti to F and/or Zr to F and/or Si to F lies in the range from 1:1 to 1:6, and the treatment solution further contains at least 0.005 g/L, preferably at least 0.01 g/L, and up to 20 g/L, preferably up to 1 g/L of organic polymers.
  6. The method according to claim 5, characterized in that the organic polymers are selected from homo- and co-polymers of vinylpyrrolidone.
  7. The method according to one or more of claims 4 to 6, characterized in that the aqueous acid treatment solution with a temperature in the range from 20 to 45°C, preferably from 30 to 40°C is brought into contact with the cleaned assembled component for a period of time in the range from 1 to 5 minutes, preferably 2 to 3 minutes.
  8. The method according to one or more of claims 1 to 7, characterized in that the aqueous acid treatment solution does not contain any other sub-group metals (transition metals) except for those of the fourth subgroup of the periodic system.
  9. The method according to one or more of claims 1 to 8, characterized in that in partial step e), the metal component is coated with a lacquer which is selected from dipping lacquer, electro-dipping lacquer, or powder lacquer.
  10. A lacquered component containing galvanized steel metal parts, which may be obtained in accordance with method according to one or more of claims 1 to 9.
  11. The use of a aqueous acid treatment solution containing at least 0.01 g/L and up to 10 g/L of Ti and/or Zr and/or Si ions as well as at least an amount of fluoride such that the atomic ratio of Ti to F and/or Zr to F and/or Si to F lies in the range from 1:1 to 1:6, and which further contains at least 0.005 g/L, and up to 1 g/L of organic polymers for a method for manufacturing a lacquered component containing metal parts in galvanized steel, wherein
    a) sheets in galvanized steel, which bear a coating based on organic polymers, are cut and/or punched and/or deformed and the thereby obtained metal parts are assembled for manufacturing the component, regions of the metal surface of the galvanized steel being formed which are not covered by the coating based on organic polymers and which have a surface ratio of steel to zinc which is greater than 9:1;
    b) the assembled component is cleaned,
    c) the cleaned assembled component is brought into contact with an aqueous chromium-free acid treatment solution, which produces on the regions of the metal surface formed in partial step a), which are not covered by the coating based on organic polymers, a passivation layer which does not represent a zinc phosphate layer,
    d) if desired, but not mandatorily, the component treated in partial step c) is rinsed one or several times with water and
    e) is coated with a lacquer coating,
    wherein all the metal parts of the component during the execution of the partial steps b) to e) exclusively consist of the sheets in galvanized steel, which bear a coating based on organic polymers, and wherein the partial step c) is the only treatment step after the partial step a), which produces a passivation layer on the regions of the metal surface formed in partial step a), which are not covered by the coating based on organic polymers.
EP04022644A 2003-11-14 2004-09-23 Supplementary corrosion protection for pieces of organic pre-coated metal sheets Expired - Lifetime EP1531012B1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10125424B2 (en) 2012-08-29 2018-11-13 Ppg Industries Ohio, Inc. Zirconium pretreatment compositions containing molybdenum, associated methods for treating metal substrates, and related coated metal substrates

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9347134B2 (en) 2010-06-04 2016-05-24 Prc-Desoto International, Inc. Corrosion resistant metallate compositions
MY169256A (en) 2012-08-29 2019-03-19 Ppg Ind Ohio Inc Zirconium pretreatment compositions containing lithium, associated methods for treating metal substrates, and related coated metal substrates
DE102015206812A1 (en) * 2015-04-15 2016-10-20 Henkel Ag & Co. Kgaa Polymer-containing pre-rinse before a conversion treatment
MX2019001874A (en) 2016-08-24 2019-06-06 Ppg Ind Ohio Inc CLEANING COMPOSITION CONTAINING IRON.
CN107012418A (en) * 2017-04-07 2017-08-04 浙江梅轮电梯股份有限公司 A kind of elevator galvanized steel plain sheet and its manufacture method

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5129967A (en) * 1988-05-03 1992-07-14 Betz Laboratories, Inc. Composition and method for non-chromate coating of aluminum
US4992116A (en) * 1989-04-21 1991-02-12 Henkel Corporation Method and composition for coating aluminum
DE19748764A1 (en) * 1997-11-05 1999-05-06 Henkel Kgaa Conductive, organic coatings
DE10005113A1 (en) * 2000-02-07 2001-08-09 Henkel Kgaa Corrosion inhibitor and corrosion protection method for metal surfaces
DE10010758A1 (en) * 2000-03-04 2001-09-06 Henkel Kgaa Corrosion protection of zinc, aluminum and/or magnesium surfaces such as motor vehicle bodies, comprises passivation using complex fluorides of Ti, Zr, Hf, Si and/or B and organic polymers
DE10022075A1 (en) * 2000-05-06 2001-11-08 Henkel Kgaa Conductive and weldable corrosion protection composition for metal surfaces in coil coating comprises a conductive pigment of zinc, aluminum, graphite, molybdenum sulfide, carbon or iron phosphide.
DE10131723A1 (en) * 2001-06-30 2003-01-16 Henkel Kgaa Corrosion protection agents and corrosion protection processes for metal surfaces

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10125424B2 (en) 2012-08-29 2018-11-13 Ppg Industries Ohio, Inc. Zirconium pretreatment compositions containing molybdenum, associated methods for treating metal substrates, and related coated metal substrates
US10920324B2 (en) 2012-08-29 2021-02-16 Ppg Industries Ohio, Inc. Zirconium pretreatment compositions containing molybdenum, associated methods for treating metal substrates, and related coated metal substrates

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