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EP2449149B1 - Traitement de protection anticorrosion pour des surfaces à base de zinc et d'alliages de zinc - Google Patents

Traitement de protection anticorrosion pour des surfaces à base de zinc et d'alliages de zinc Download PDF

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Publication number
EP2449149B1
EP2449149B1 EP10728680A EP10728680A EP2449149B1 EP 2449149 B1 EP2449149 B1 EP 2449149B1 EP 10728680 A EP10728680 A EP 10728680A EP 10728680 A EP10728680 A EP 10728680A EP 2449149 B1 EP2449149 B1 EP 2449149B1
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Prior art keywords
acid
treatment solution
process according
acids
group
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EP2449149A1 (fr
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Udo Hofmann
Hermann Donsbach
Jörg UNGER
Volker Krenzel
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Atotech Deutschland GmbH and Co KG
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Atotech Deutschland GmbH and Co KG
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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/12Orthophosphates containing zinc cations
    • C23C22/17Orthophosphates containing zinc cations containing also organic acids
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/82After-treatment
    • C23C22/83Chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C2222/00Aspects relating to chemical surface treatment of metallic material by reaction of the surface with a reactive medium
    • C23C2222/10Use of solutions containing trivalent chromium but free of hexavalent chromium

Definitions

  • the invention relates to the corrosion protection of metallic materials, in particular of those which are provided with a surface of zinc or zinc alloys.
  • the coating of the metallic workpiece to be protected with a coating of another metal is a widely used and established method in the art.
  • the coating metal can behave in the corrosive medium either electrochemically nobler or less noble than the material base metal. If the coating metal behaves less noble, it acts in the corrosive medium compared to the base metal as a sacrificial anode (cathodic corrosion protection).
  • this protective function associated with the formation of corrosion products of the coating metal is thus desired, the corrosion products of the coating often lead to undesirable decorative and often also to functional impairments of the workpiece.
  • cathodically protective base coating metals such as, for example, Zinc or aluminum and their alloys often used so-called conversion coatings.
  • conversion coatings These are reaction products of the non-noble coating metal which are insoluble in aqueous media over a wide pH range with the treatment solution. Examples of these so-called conversion layers are so-called phosphating and chromating.
  • chromium (VI) ions see EP 0 553 164 A1 .
  • chromium (VI) is reduced to chromium (III), which in the surface film which is more alkaline due to the evolution of hydrogen, inter alia as chromium (III) hydroxide or sparingly soluble ⁇ -oxo or ⁇ -hydroxo bridging Chromium (III) complex is deposited.
  • chromium (III) hydroxide or sparingly soluble ⁇ -oxo or ⁇ -hydroxo bridging Chromium (III) complex is deposited.
  • sparingly soluble zinc chromate (VI) is formed. Overall, a tightly closed, very well protects against corrosion attack by electrolytes conversion coating on the zinc surface.
  • chromium (VI) compounds are acutely toxic and highly carcinogenic, requiring replacement of the methods associated with these compounds.
  • a disadvantage of this additional process step is the occurrence of drainage drops in the coating of workpieces made on the frame and / or the bonding of coated bulk material; In addition, problems such as dimensional accuracy of threads and the like, which are associated with the layer thickness of these seals arise.
  • the font EP 0 479 289 A1 describes a chromating process in which the substrates are immersed in a treatment solution containing, in addition to chromium (VI) and chromium (III) ions, hydrofluoric acid and phosphoric acid, a silane coupling agent.
  • the patent EP 0 922 785 B1 describes a treatment solution and a process for the production of protective layers on metals, wherein the surface to be protected with a treatment solution, the chromium (III) ions, an oxidizing agent and an oxyacid or an oxyacid salt of phosphorus or a corresponding anhydride contains.
  • This treating solution may further contain a monomeric silane coupling agent.
  • EP 1 051 539 B1 describes a treatment solution for increasing the corrosion protection of substrates which, in addition to chromium (VI) and chromium (III) ions, also contains phosphoric acid, hydrofluoric acid, colloidal silicon dioxide and a monomeric epoxy-functionalized silane.
  • the font WO 2008/14166 A1 describes a treatment solution for the production of anticorrosive coatings.
  • This treatment solution contains, in addition to zinc ions, phosphoric acid or acidic phosphates, organic or inorganic anions which one of the elements boron, silicon, titanium or zirconium, trivalent chromium ions and an inorganic or organic peroxide as an oxidizing agent.
  • the font WO 97/15700 A1 describes a treatment solution for the production of anticorrosive coatings.
  • the treatment solution contains hydrolyzed silanes and phosphoric acid and is free of chromium ions and chromium containing compounds.
  • the invention has for its object to provide methods for increasing the corrosion protection of metallic, especially zinc-containing and zinc-containing, provided with a conversion layer, surfaces.
  • the aim is to preserve or improve the decorative and functional properties of the surfaces.
  • the above problems with the use of chromium (VI) -containing compounds and hydrofluoric acid or post-treatments for sealing are to be avoided.
  • the process usually carried out in two separate stages is to apply a passivation step containing chromium (III) ions followed by a one-step process be replaced, in which the functionality of a chromium (III) ion-containing passivation layer and a sealing are combined.
  • a further aspect of the invention is that it is possible to dispense with the rinsing steps which are normally required in the two-stage processes known from the prior art between the application of the passivation containing chromium (III) ions and the sealing. This significantly reduces the amount of heavy metal contaminated wastewater. Furthermore, the handling of silanes and other metal alkoxides should be made controllable by separately prepared under appropriate reaction conditions organosols of sufficient stability and film-forming properties and then only with the remaining components of the treatment solution (chromium (III) ions, phosphate source and other optional components) be mixed.
  • Phosphate compounds are derived from phosphorus in the oxidation state + V derived oxo compounds and their esters with organic radicals having up to 12 carbon atoms and the salts of mono- and diesters.
  • Suitable phosphate compounds are in particular alkyl phosphates with alkyl groups having up to 12 carbon atoms.
  • Suitable phosphate compounds are ortho-phosphoric acid (H 3 PO 4 ) and its salts, polyphosphoric acid and its salts, meta-phosphoric acid and its salts, phosphoric acid methyl esters (mono-, di- and triesters), phosphoric acid ethyl esters (mono-, di- and triesters ), N- propyl phosphate (mono-, di- and triester), isopropyl orthophosphate (mono-, di- and triester), n- butyl phosphate (mono-, di- and triester), 2-butyl phosphoric acid (mono -, di- and triesters), phosphoric acid tert -butyl ester (mono-, di- and triesters), the salts of said mono- and diesters and di- phosphorus pentoxide and mixtures of these compounds.
  • salts includes not only the salts of completely deprotonated acids, but salts in all possible protonation
  • the treating solution preferably contains between 0.2 g / l and 20 g / l of chromium (III) ions, more preferably between 0.5 g / l and 15 g / l of chromium (III) ions and more preferably between 1 g / l and 10 g / l chromium (III) ions.
  • the ratio of the molar concentration of chromium (III) ions to the molar concentration of the at least one phosphate compound (based on orthophosphate) is between 1: 1.5 and 1: 3, preferably between 1: 1.7 and 1: 2.5.
  • Chromium (III) ions may be added to the treatment solution either in the form of inorganic chromium (III) salts such as basic chromium (III) sulfate, chromium (III) hydroxide, chromium (III) dihydrogen phosphate, chromium (III) chloride , Chromium (III) nitrate, potassium chromium (III) sulfate or Chromium (III) salts of organic acids such as chromium (III) methanesulfonate, chromium (III) citrate are added or produced by reduction of suitable chromium (VI) compounds in the presence of suitable reducing agents.
  • inorganic chromium (III) salts such as basic chromium (III) sulfate, chromium (III) hydroxide, chromium (III) dihydrogen phosphate, chromium (III) chloride , Chromium (III) nitrate, potassium chromium
  • Suitable chromium (VI) compounds are, for example, chromium (VI) oxide, chromates such as potassium or sodium chromate, dichromates such as, for example, potassium or sodium dichromate.
  • Suitable reducing agents for the in situ generation of chromium (III) ions are, for example, sulfites such as sodium sulfite, sulfur dioxide, phosphites such as sodium hypophosphite, phosphorous acid, hydrogen peroxide, methanol, hydroxycarboxylic acids and hydroxydicarboxylic acids such as gluconic acid, citric acid and malic acid.
  • the treatment solution preferably has a pH between pH 2 and pH 7, more preferably between pH 2.5 and pH 6, and most preferably between pH 2.5 and pH 3.
  • the above-mentioned organosol can be obtained by per se known hydrolysis and condensation of the at least one alkoxysilane of the formula (1).
  • Particularly preferred among the above alkoxysilanes of the formula (1) is at least one in which at least one R has a group which can undergo a polyaddition (including polymerization) or polycondensation reaction.
  • This grouping capable of polyaddition or polycondensation reaction is preferably an epoxy group or carbon-carbon multiple bonds, with a (meth) acrylate group being a particularly preferred example of the latter groupings.
  • Particularly preferred alkoxysilanes according to formula (1) are those in which x is 2 or 3 and in particular 3 and a radical R is ⁇ -glycidyloxy-C 2-6 -alkyl or ⁇ - (meth) acryloxy-C 2-6 - Alkyl stands.
  • alkoxysilanes are 3-glycidoxypropyltri (m) ethoxysilane, 3,4-epoxybutyltri (m) ethoxysilane and 2- (3,4-epoxycyclohexyl) ethyltri (m) ethoxysilane, 3- (meth) acryloxypropyltri (m) ethoxysilane and 2- (Meth) acryloxyethyltri (m) ethoxysilane, 3-glycidoxypropyldimethyl (m) ethoxysilane, 3-glycidoxypropylmethyldi (m) ethoxysilane, 3- (meth) acryloxypropylmethyldi (m) ethoxysilane and 2- (meth) acryloxyethylmethyl-di (m) ethoxysilane.
  • alkoxysilanes of the formula (1) which can preferably be used in combination with alkoxysilanes having the above groupings capable of polyaddition or polycondensation reaction are, for example, hexadecyltri (m) ethoxysilane, cyclohexyltri (m) ethoxysilane, cyclopentyltri (m) ethoxysilane, ethyltri (m) ethoxysilane, phenylethyltri (m) ethoxysilane, phenyltri (m) ethoxysilane, n-propyltri (m) ethoxysilane, cyclohexyl (m) ethyldimethoxysilane, dimethyldi (m) ethoxysilane, diisopropyldi (m) ethoxysilane and phenylmethyldi (m) ethoxysilane.
  • At least one alkoxide according to formula (2) is then combined with the hydrolyzate of the at least one alkoxysilane of formula (1).
  • the alkoxides according to formula (2) are very reactive, so that in the absence of a complexing agent, the components according to formulas (1) and (2) would hydrolyze and condense very rapidly on contact with water. According to the invention, however, it is not necessary to use the reactive alkoxides directly in complexed form. Rather, it is possible to add the complexing agent or compounds shortly after the start of the reaction of the components according to formulas (1) and (2).
  • alkoxides according to formula (2) are aluminum sec-butoxide, titanium isopropoxide, titanium propoxide, titanium butoxide, zirconium isopropoxide, zirconium propoxide, zirconium butoxide, zirconium ethoxide, tetraethoxysilane, tetramethoxysilane, tetrapropyloxysilane and tetrabutyloxysilane.
  • complexing agents are ethanolamines and alkyl phosphates, such as tri-, diethanolamine and butyl phosphate.
  • examples of such complexed alkoxides according to formula (2) are titanium acetylacetonates, titanium bisacetoacetates, triethanolamine titanates, triethanolamine zirconates and zirconium diethyl citrates.
  • the complexing agent in particular a chelate compound, causes some complexation of the metal cation, so that the hydrolysis and condensation rate of the components according to formulas (1) and (2) is reduced.
  • the organosol comprises a water-compatible or water-miscible solvent having a boiling point of at least 150 ° C.
  • a water-compatible or water-miscible solvent having a boiling point of at least 150 ° C.
  • diethylene glycol, triethylene glycol, butyl diglycol, propylene glycols, butylene glycols, and polyethylene glycols can be used therefor.
  • the object of the high-boiling solvents is that improved resistance of the organosols can be achieved in exchange for the liberated during hydrolysis low molecular weight alcohol.
  • the organosol is characterized in that the weight ratio of the component according to formula (1) to the component according to formula (2) in the range 1 to 1 to 1 to 100, particularly preferably in the range 1 to 1 to 1 to 25 lies. Since the components according to formula (2) also serve as crosslinking agents for the alkoxysilanes according to formula (1), they should be present in the organosols at least in equimolar amounts relative to the component of formula (1).
  • the organosol is the treatment solution according to the invention based on an active ingredient content of 25% in the organosol in an amount of 1 g / l to 50 g / l, preferably 3 g / l to 20 g / l and most preferably 5 g / l to 15 g / l added.
  • the treatment solution may additionally (optionally) contain one or more further complexing agents.
  • Suitable further complexing agents are, in particular, organic chelate ligands.
  • suitable further complexing agents are polycarboxylic acids, hydroxycarboxylic acids, hydroxypolycarboxylic acids, aminocarboxylic acids or hydroxyphosphonic acids.
  • carboxylic acids examples include citric acid, tartaric acid, malic acid, lactic acid, gluconic acid, Glucuronic acid, ascorbic acid, isocitric acid, gallic acid, glycolic acid, 3-hydroxypropionic acid, 4-hydroxybutyric acid, salicylic acid, nicotinic acid, alanine, glycine, asparagine, aspartic acid, cysteine, glutamic acid, glutamine, lysine.
  • Suitable hydroxyphosphonic acids are, for example, Dequest 2010 TM (from Solutia, Inc.); suitable as aminophosphonic acids, for example Dequest 2000 TM (from Solutia, Inc.).
  • the treatment solution will contain at least one metal or metalloid, e.g. Sc, Y, Ti, Zr, Mo, W, Mn, Fe, Co, Ni, Zn, B, Al, Si.
  • metal or metalloid e.g. Sc, Y, Ti, Zr, Mo, W, Mn, Fe, Co, Ni, Zn, B, Al, Si.
  • These elements may be added in the form of their salts or in the form of complex anions or the corresponding acids of these anions such as hexafluoroboric acid, hexafluorosilicic acid, hexafluorotitanic acid or hexafluorozirconic acid, tetrafluoroboric acid or hexafluorophosphoric acid or their salts.
  • zinc which may be added in the form of zinc (II) salts, for example zinc sulfate, zinc chloride, zinc phosphate, zinc oxide or zinc hydroxide.
  • the treatment solution is added between 0.5 g / l and 25 g / l, more preferably between 1 g / l and 15 g / l Zn 2+ .
  • the list of zinc compounds are only examples of compounds suitable according to the invention, but does not limit the amount of suitable zinc compounds to the substances mentioned.
  • the treatment solution may additionally (optionally) contain one or more water-soluble or water-dispersible polymers selected from the group consisting of polyethylene glycols, polyvinylpyrrolidones, polyvinyl alcohols to improve the film formation on the surface to be treated and to increase the hydrophobicity of the surface.
  • polyethylene glycols polyvinylpyrrolidones
  • polyvinyl alcohols polyvinyl alcohols
  • the concentration of the at least one polymer is preferably in the range between 50 mg / l and 20 g / l.
  • the treatment solution may additionally (optionally) contain one or more wetting agents.
  • one or more wetting agents may additionally (optionally) contain one or more wetting agents.
  • fluoroaliphatic polymeric esters such as e.g. Fluorad FC-4432 TM (from 3M).
  • the treatment solution may additionally (optionally) contain one or more lubricants.
  • Suitable lubricants are, for example, polyether-modified siloxanes, polyether wax emulsions, ethoxylated alcohols, PTFE, PVDF, ethylene copolymers, paraffin emulsions, polypropylene wax emulsions, MoS 2 and dispersions thereof, WS 2 and emulsions thereof, polyethylene glycols, polypropylene, Fischer-Tropsch hard waxes, micronized and synthetic hard waxes, Graphite, metal soaps and polyurea.
  • Particularly preferred lubricants are PTFE, micronized hard waxes and polyether wax emulsions.
  • the optional lubricants are added in an amount of 0.1 g / l to 300 g / l, preferably 1 g / l to 30 g / l of the treatment solution according to the invention.
  • the surfaces treated according to the invention are metallic, preferably zinc-containing, and zinc-containing surfaces which are optionally provided with a chromium (III) -containing conversion layer.
  • a layer is deposited on the treated surface which contains chromium (III) ions, phosphate (s), a silicon / metal-organic network and optionally further metal ions, such as e.g. Zinc ions, and optionally one or more polymeric components.
  • the contacting of the treatment solution with the surface to be treated can be carried out in the inventive method according to known methods, in particular by immersion.
  • the temperature of the treatment solution is preferably between 10 ° C and 90 ° C, more preferably between 20 ° C and 80 ° C, more preferably between 25 ° C and 50 ° C.
  • the duration of the contacting is preferably between 0.5 s and 180 s, more preferably between 5 s and 60 s, most preferably between 10 s and 30 s.
  • the treatment solution can be prepared prior to carrying out the method according to the invention by dilution of a correspondingly higher concentrated concentrate solution.
  • the objects treated according to the invention are no longer rinsed after contacting, but are dried directly.
  • the process according to the invention leads to increased corrosion protection in the case of articles which have a zinc-containing surface.
  • the method of the invention may also be used.
  • the method according to the invention after application of a so-called conversion layer is applied to full metal zinc and zinc alloy surfaces.
  • Conversion layers can be deposited from treatment solutions containing, for example, chromium (III) ions and an oxidizing agent.
  • the method of the present invention is applied to full metal zinc and zinc alloy surfaces after oxidative activation.
  • This oxidative activation is, for example, immersing the galvanized substrate in an aqueous solution containing an oxidizing agent.
  • Suitable oxidizing agents for this purpose are nitrates and nitric acid, peroxides such as hydrogen peroxide, persulfates and perborates.
  • zinc flake coatings the process according to the invention is applied directly after application and curing of the zinc flake coating.
  • Sample parts made of steel were first coated in a weakly acidic electroplating process (Unizinc ACZ 570 from Atotech GmbH) with an 8-10 ⁇ m thick zinc coating and rinsed with demineralized water.
  • a weakly acidic electroplating process Unizinc ACZ 570 from Atotech GmbH
  • sample parts were provided with a chromium (III) ion and nitrate-containing conversion layer (EcoTri® HC2 from Atotech Deutschland GmbH) and dried.
  • a chromium (III) ion and nitrate-containing conversion layer (EcoTri® HC2 from Atotech Deutschland GmbH)
  • treatment solution A a treatment solution with a pH of 3.9 was applied, which contained the following constituents: 4.5 g / l Cr 3+ from chromium (III) hydroxide 18 g / l PO 4 3- from ortho-phosphoric acid 5.5 g / l Zn 2+ from zinc oxide 11 g / l citric acid
  • the corrosion resistance formation of red corrosion according to EN ISO 9227 was tested with a neutral salt spray test. The formation of red corrosion was observed after 864 h.
  • Sample parts made of steel were coated in a weakly acidic galvanic process (Unizinc ACZ 570 from Atotech GmbH) with an 8-10 ⁇ m thick zinc coating and rinsed with demineralized water.
  • a weakly acidic galvanic process Unizinc ACZ 570 from Atotech GmbH
  • sample parts were provided with a chromium (III) ion and nitrate-containing conversion layer (EcoTri®HC2 from Atotech Deutschland GmbH) and dried.
  • a chromium (III) ion and nitrate-containing conversion layer (EcoTri®HC2 from Atotech Deutschland GmbH)
  • a treatment solution according to the invention with a pH value of 2.8 was applied, which contained the following constituents: 4.5 g / l Cr 3+ from chromium (III) hydroxide 18 g / l PO 4 3- from ortho-phosphoric acid 5.5 g / l Zn 2+ from zinc oxide 11 g / l citric acid 50 g / l an organosol having an active substance content of 25% (in% by weight) which has been prepared from tetraethoxysilane as alkoxysilane according to formula (1) and 3-glycidyloxypropyltriethoxysilane as metal alkoxide according to formula (2).
  • the corrosion resistance formation of red corrosion according to EN ISO 9227 was tested with a neutral salt spray test. The formation of red corrosion was observed after 1500 h.
  • Sample parts made of steel were coated with a zinc flake-containing treatment solution (Zintek® 800 WD 1 from Atotech Deutschland GmbH) with a 10 ⁇ m thick zinc flake-containing overlay.
  • a zinc flake-containing treatment solution Zintek® 800 WD 1 from Atotech GmbH
  • Example 1 the treatment solution of Example 1 according to the invention was applied and the sample parts coated in this way were dried.
  • the corrosion resistance formation of red corrosion according to EN ISO 9227 was tested with a neutral salt spray test. The formation of red corrosion was observed after 3500 hours.

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

Claims (15)

  1. Procédé pour la production d'une couche de recouvrement de protection contre la corrosion, une surface à traiter étant mise en contact avec une solution de traitement aqueuse, qui contient
    - des ions de chrome (III),
    - au moins un composé de type phosphate et
    - un organosol préparé par hydroxyle et condensation, qui est obtenu par réaction d'un ou de plusieurs alcoxysilanes de formule (1)

            R4-xSi(OR1)x     (1)

    les radicaux R étant identiques ou différents les uns des autres et représentant à chaque fois un groupe hydrocarboné substitué ou non substitué comprenant 1 à 22 atomes de carbone et x valant 1, 2 ou 3 et R1 représentant un groupe hydrocarboné substitué ou non substitué comprenant 1 à 8 atomes de carbone, et d'un ou de plusieurs alcoxydes de formule (2)

            Me(OR2)n     (2)

    Me représentant Ti, Zr, Hf, Al, Si et n représentant l'étage d'oxydation de Me et R2 étant choisi parmi les groupes hydrocarbonés substitués ou non substitués qui contiennent 1 à 8 atomes de carbone,
    la solution de traitement aqueuse étant exempte de peroxydes inorganiques et organiques.
  2. Procédé selon la revendication 1, le rapport de la concentration en masse d'ions de chrome (III) à la concentration en masse dudit au moins un composé de type phosphate dans la solution de traitement aqueuse (par rapport à l'orthophosphate) étant situé entre 1:1,5 et 1:3.
  3. Procédé selon l'une quelconque des revendications 1 et 2, ledit au moins un composé de type phosphate dans la solution de traitement aqueuse étant choisi dans le groupe constitué par l'acide orthophosphorique, les acides polyphosphoriques, l'acide métaphosphorique, les sels de ces acides, les esters de ces acides avec des radicaux organiques comprenant jusqu'à 12 atomes de carbone ainsi que les mélanges de ces composés.
  4. Procédé selon l'une quelconque des revendications 1 à 3, la concentration en ions de chrome (III) dans la solution de traitement aqueuse étant située dans la plage entre 0,2 g/l et 20 g/l.
  5. Procédé selon l'une quelconque des revendications 1 à 4, ledit au moins un alcoxysilane selon la formule (1) étant choisi dans le groupe constitué par les trialcoxysilanes et les dialcoxysilanes et R1 représentant des groupes hydrocarbonés identiques ou différents liés via un atome de carbone à l'atome de silicium, le cas échéant ramifiés, qui sont interrompus par de l'oxygène, de l'azote ou le groupe NR2, R2 représentant hydrogène ou C1-C6-alkyle et pouvant porter un ou plusieurs substituants, choisis dans le groupe des halogènes et des groupes portant des fonctions amino, amido, carboxy, acryloxy, méthacryloxy et époxy.
  6. Procédé selon l'une quelconque des revendications 1 à 5, ledit au moins un alcoxysilane selon la formule (1) étant choisi dans le groupe constitué par le 3-glycidoxypropyltriméthoxysilane, le 3-glycidoxypropyltriéthoxysilane, le 3,4-époxybutyltriméthoxysilane, le 3,4-époxybutyltriéthoxysilane, le 2-(3,4-époxycyclohexyl)éthyltriméthoxysilane et le 2-(3,4-époxycyclohexyl)éthyltriéthoxysilane.
  7. Procédé selon l'une quelconque des revendications 1 à 6, Me dans au moins un composé de formule (2) étant le silicium.
  8. Procédé selon l'une quelconque des revendications 1 à 7, l'organosol contenant un solvant miscible à l'eau présentant un point d'ébullition d'au moins 150°C.
  9. Procédé selon l'une quelconque des revendications 1 à 8, l'organosol contenant en outre un ou plusieurs complexants, choisis dans le groupe constitué par les acides carboxyliques saturés et insaturés, les composés 1,3-dicarbonyle, les éthanolamines, les alkylphosphates, les acides polycarboxyliques, les hydroxycarboxyliques, les acides hydroxypolycarboxyliques, les acides aminocarboxyliques ou les acides hydroxyphosphoniques et les acides aminophosphoniques.
  10. Procédé selon l'une quelconque des revendications 1 à 9, la solution de traitement aqueuse contenant au moins un autre complexant, qui est choisi dans le groupe constitué par l'acide acétique, l'acide méthacrylique, l'acétylacétone, l'ester éthylique de l'acide acétoacétique, la triéthanolamine, la diéthanolamine, le butylphosphate, l'acide citrique, l'acide tartrique, l'acide malique, l'acide lactique, l'acide gluconique, l'acide glucuronique, l'acide ascorbique, l'acide isocitrique, l'acide gallique, l'acide glycolique, l'acide 3-hydroxypropionique, l'acide 4-hydroxybutyrique, l'acide salicylique, l'acide nicotinique, l'alanine, la glycine, l'asparagine, l'acide aspartique, la cystéine, l'acide glutamique, la glutamine et la lysine.
  11. Procédé selon l'une quelconque des revendications 1 à 10, la solution de traitement contenant en outre un ou plusieurs polymères solubles ou dispersibles dans l'eau, choisis dans le groupe constitué par les polyéthylèneglycols, les polypropylèneglycols, les polyvinylpyrrolidones, les poly(alcools vinyliques), les poly(acides itaconiques), les polyacrylates et les copolymères des monomères à chaque fois à leur base.
  12. Procédé selon l'une quelconque des revendications 1 à 11, la solution de traitement aqueuse contenant en plus au moins un lubrifiant.
  13. Procédé selon l'une quelconque des revendications 1 à 12, la solution de traitement aqueuse contenant en plus un ou plusieurs métaux ou métalloïdes, choisis dans le groupe constitué par Sc, Y, Ti, Zr, Mo, W, Mn, Fe, Co, Ni, Zn, B, Al, Si et P.
  14. Procédé selon la revendication 13, le métal ou le métalloïde étant ajouté à la solution de traitement sous forme d'un de ses sels ou sous forme d'un anion complexe ou des acides correspondants de ces anions, tels que l'acide hexafluoroborique, l'acide hexafluorosilicique, l'acide hexafluorotitanique ou l'acide hexafluorozirconique, l'acide tétrafluoroborique ou l'acide hexafluorophosphorique ou leurs sels.
  15. Procédé selon l'une quelconque des revendications 1 à 14, le pH de la solution de traitement aqueuse étant situé entre pH 1,5 et pH 9.
EP10728680A 2009-07-03 2010-07-05 Traitement de protection anticorrosion pour des surfaces à base de zinc et d'alliages de zinc Active EP2449149B1 (fr)

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EP09164575A EP2281923A1 (fr) 2009-07-03 2009-07-03 Traitement de protection anticorrosion pour surfaces en zinc et alliages de zinc
PCT/EP2010/059586 WO2011000969A1 (fr) 2009-07-03 2010-07-05 Traitement de protection anticorrosion pour des surfaces à base de zinc et d'alliages de zinc
EP10728680A EP2449149B1 (fr) 2009-07-03 2010-07-05 Traitement de protection anticorrosion pour des surfaces à base de zinc et d'alliages de zinc

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Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2576861B1 (fr) * 2010-05-26 2014-11-26 Atotech Deutschland GmbH Procédé pour la formation de couches de protection contre la corrosion sur des surfaces métalliques
TWI555880B (zh) * 2011-04-01 2016-11-01 迪普索股份有限公司 3價鉻化學轉換被膜用整理加工劑及黑色3價鉻化學轉換被膜之整理加工方法
EP2773795B1 (fr) * 2011-11-03 2015-10-14 Basf Se Préparation permettant la passivation de surfaces métalliques contenant des polymères chargés en groupe acide et des composés ti ou zr
CN104073075B (zh) * 2013-09-05 2016-07-06 攀钢集团攀枝花钢铁研究院有限公司 一种三价铬涂料及其制备方法和热镀金属材料
DE202013010956U1 (de) 2013-09-13 2014-12-17 Ewh Industrieanlagen Gmbh & Co. Kg Behandlungslösung für ein Verfahren zum Erzeugen einer korrosionsschützenden Überzugsschicht und Konzentrat einer solchen Behandlungslösung
DE102013015114A1 (de) 2013-09-13 2015-03-19 Ewh Industrieanlagen Gmbh & Co. Kg Verfahren zur Erzeugung einer korrosionsschützenden Überzugsschicht auf einer Metalldispersionstrockenschicht oder auf einer Oberfläche eines μm-skalierten Metallteilchen und Verwendung einer Behandlungslösung zur Durchführung eines solchen Verfahrens
ES2732264T5 (en) 2014-02-13 2025-06-26 Doerken Ewald Ag Method for production of a substrate with a chromium vi free and cobalt-free passivation
CN104846359B (zh) * 2014-02-17 2017-12-29 广州中国科学院工业技术研究院 用于金属表面预处理的复合处理剂及其制备方法和应用
KR101792240B1 (ko) * 2015-09-18 2017-10-31 주식회사 포스코 편면도금 강판의 표면처리용 조성물, 이를 이용하여 표면처리된 강판, 및 이를 이용한 표면처리 방법
CN105937031B (zh) * 2016-06-29 2018-10-30 周少霞 一种热镀锌板用钝化液的制备方法
JP6870983B2 (ja) * 2016-12-27 2021-05-12 日本ペイント・サーフケミカルズ株式会社 亜鉛系メッキ鋼板用表面処理剤
PT3360989T (pt) * 2017-02-13 2019-04-02 Atotech Deutschland Gmbh Método para passivar eletroliticamente uma camada de crómio exterior ou de liga de crómio exterior para aumentar a sua resistência à corrosão
JP6375043B1 (ja) 2017-10-31 2018-08-15 日本パーカライジング株式会社 前処理剤、前処理方法、化成皮膜を有する金属材料およびその製造方法、並びに塗装金属材料およびその製造方法
CN108034935A (zh) * 2017-12-12 2018-05-15 广州旭淼新材料科技有限公司 一种无铬转化成膜液及其制备方法
CN108193202B (zh) * 2017-12-29 2020-07-31 南京科润工业介质股份有限公司 一种环保型金属表面处理剂及其应用
RU2758664C1 (ru) 2018-01-30 2021-11-01 Прк-Десото Интернэшнл, Инк. Системы и способы для обработки металлической подложки
EP3569734A1 (fr) 2018-05-18 2019-11-20 Henkel AG & Co. KGaA Composition de passivation à base de chrome trivalent
CN109338348B (zh) * 2018-10-24 2019-09-20 河南恒润昌环保科技有限公司 一种无磷水性金属硅烷处理剂及其制备方法
EP3663435B1 (fr) 2018-12-05 2024-03-13 Henkel AG & Co. KGaA Composition de passivation basée sur des mélanges d'acides phosphorique et phosphonique
EP4506429A3 (fr) * 2020-06-10 2025-05-14 Novelis Inc. Compositions de prétraitement liées à des substrats métalliques et leurs procédés de fabrication
EP3964609A1 (fr) 2020-08-28 2022-03-09 Coventya SAS Produit électroplaqué et procédé de préparation de tels produits par traitement à haute température
US11746294B2 (en) * 2021-05-28 2023-09-05 Chemtreat, Inc. Corrosion control using organic filmers and passivators in systems for processing nitrogen-containing solutions
CN115613022B (zh) * 2022-09-28 2024-08-16 湖南金裕环保科技有限公司 铝及铝合金无铬本色钝化剂及其制备方法

Family Cites Families (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3392008B2 (ja) * 1996-10-30 2003-03-31 日本表面化学株式会社 金属の保護皮膜形成処理剤と処理方法
JPS5935684A (ja) * 1982-08-20 1984-02-27 Nippon Steel Corp 金属表面処理組成物
JPS6160766A (ja) * 1984-08-31 1986-03-28 Kansai Paint Co Ltd 潤滑性塗膜形成用水系組成物
JPS6283478A (ja) * 1985-10-09 1987-04-16 Sumitomo Metal Ind Ltd 塗装密着性に優れたクロメ−ト処理鋼材
JPH0730457B2 (ja) * 1988-02-18 1995-04-05 新日本製鐵株式会社 クロメート処理メッキ鋼板とその製造方法
JPH03146676A (ja) * 1989-10-31 1991-06-21 Kobe Steel Ltd 耐吸湿汚れ性にすぐれるクロメート処理鋼板の製造方法
JPH0696778B2 (ja) 1990-10-05 1994-11-30 新日本製鐵株式会社 亜鉛系めっき鋼板のクロメート処理方法
JP2628782B2 (ja) 1990-10-08 1997-07-09 日本パーカライジング株式会社 亜鉛系めっき鋼板のクロメート処理方法
US5728203A (en) 1995-10-26 1998-03-17 Lord Corporation Aqueous protective and adhesion promoting composition
DE19638176A1 (de) 1996-09-18 1998-04-16 Surtec Produkte Und Systeme Fu Chrom(VI)freie Chromatschicht sowie Verfahren zu ihrer Herstellung
JPH10176281A (ja) * 1996-12-17 1998-06-30 Kawasaki Steel Corp 耐水二次密着性と電着塗装性に優れる有機複合被覆鋼板
DE19814605A1 (de) * 1998-04-01 1999-10-07 Kunz Gmbh Mittel zur Versiegelung von metallischen, insbesondere aus Zink oder Zinklegierungen bestehenden Untergründen
JP2000014755A (ja) * 1998-06-29 2000-01-18 Sumitomo Metal Ind Ltd 光触媒機能を備えた金属板
ATE243783T1 (de) 1998-12-01 2003-07-15 Po Hang Iron & Steel Oberflächenbehandeltes stahlblech für brennstofftanks und verfahren zu dessen herstellung
JP2000192251A (ja) * 1998-12-24 2000-07-11 Nisshin Steel Co Ltd クロメ−ト処理液および処理方法
JP2000199074A (ja) * 1998-12-28 2000-07-18 Nippon Parkerizing Co Ltd 希土類・鉄系焼結永久磁石の沈着型表面処理液および表面処理方法、ならびに該表面処理方法により得られた表面を有する希土類・鉄系焼結永久磁石
US6197415B1 (en) * 1999-01-22 2001-03-06 Frisby Technologies, Inc. Gel-coated materials with increased flame retardancy
FR2812307B1 (fr) 2000-07-25 2003-02-14 Chemetall S A Couche noire anticorrosive sur un alliage de zinc et son procede de preparation
US7264874B2 (en) * 2004-12-22 2007-09-04 Aps Laboratory Preparation of metal chalcogenide nanoparticles and nanocomposites therefrom
US7410631B2 (en) * 2005-03-02 2008-08-12 Aps Laboratory Metal phosphate sols, metal nanoparticles, metal-chalcogenide nanoparticles, and nanocomposites made therefrom
US10041176B2 (en) * 2005-04-07 2018-08-07 Momentive Performance Materials Inc. No-rinse pretreatment methods and compositions
US7253226B1 (en) 2005-08-11 2007-08-07 Aps Laboratory Tractable silica sols and nanocomposites therefrom
JP5213308B2 (ja) * 2006-03-08 2013-06-19 日本ペイント株式会社 金属用表面処理剤
JP4524352B2 (ja) * 2006-04-17 2010-08-18 名古屋市 防食剤及び防食剤の製造方法
JP5055822B2 (ja) * 2006-04-27 2012-10-24 住友金属工業株式会社 塗膜密着性に優れた塗装鋼板
CA2664664C (fr) * 2006-09-29 2014-06-17 Momentive Performance Materials Inc. Composition stable en stockage a base d'un condensat partiel et/ou complet d'un silane organofonctionnel hydrolysable
JP4955379B2 (ja) * 2006-12-20 2012-06-20 株式会社キャディック コーティング溶液、該溶液を用いた無機−有機ハイブリッド皮膜の形成方法、およびこの形成方法により得られる皮膜
JP2010528178A (ja) * 2007-05-24 2010-08-19 プロコート・テクノロジアス・エセエレ 無機固体粒子フリーの腐食保護性及び電気伝導性組成物、並びに金属シートの表面処理方法
JP2008111188A (ja) * 2007-09-25 2008-05-15 Hitachi Chem Co Ltd プリント配線板用の銅箔
DE102010030114B4 (de) * 2009-08-11 2021-11-04 Evonik Operations Gmbh Wässriges Silansystem für den Blankkorrosionsschutz, Verfahren zu dessen Herstellung, dessen Verwendung sowie mit diesem behandelte Gegenstände und Korrosionsschutzschicht

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CN102471890B (zh) 2014-06-18
KR20120102566A (ko) 2012-09-18
EP2281923A1 (fr) 2011-02-09
CN102471890A (zh) 2012-05-23
BR112012000037A2 (pt) 2016-03-15
JP5627680B2 (ja) 2014-11-19
ES2401173T3 (es) 2013-04-17
CA2765961A1 (fr) 2011-01-06
US8951363B2 (en) 2015-02-10
WO2011000969A1 (fr) 2011-01-06
US20120091398A1 (en) 2012-04-19
JP2012531527A (ja) 2012-12-10
EP2449149A1 (fr) 2012-05-09
KR101565203B1 (ko) 2015-11-02

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