EP1863952B1 - Composition et procede de preparation de revetements de protection sur des substrats metalliques - Google Patents

Composition et procede de preparation de revetements de protection sur des substrats metalliques Download PDF

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EP1863952B1
EP1863952B1 EP05851727A EP05851727A EP1863952B1 EP 1863952 B1 EP1863952 B1 EP 1863952B1 EP 05851727 A EP05851727 A EP 05851727A EP 05851727 A EP05851727 A EP 05851727A EP 1863952 B1 EP1863952 B1 EP 1863952B1
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compound
grams
water soluble
glycol
carboxylic
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German (de)
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EP1863952A2 (fr
EP1863952A4 (fr
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Craig A. Matzdorf
William C. Nickerson, Jr.
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US Department of Navy
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US Department of Navy
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Priority claimed from US11/076,106 external-priority patent/US20060180247A1/en
Priority claimed from US11/058,715 external-priority patent/US20100032060A1/en
Priority claimed from US11/116,165 external-priority patent/US7811391B2/en
Priority claimed from US11/116,166 external-priority patent/US20060240191A1/en
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Publication of EP1863952A4 publication Critical patent/EP1863952A4/fr
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • 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
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C21/00Alloys based on aluminium
    • 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
    • C23C22/73Chemical 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 characterised by the process
    • C23C22/77Controlling or regulating of the coating process
    • 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

  • This invention relates to compositions and to a process for using said compositions for preparing protective coatings on various metal substrates.
  • the process comprises treating the metal substrates with effective amounts of an acidic aqueous solution containing at least one trivalent chromium compound, at least one fluorozirconate, at least one carboxylic compound and/or polyhydroxy compound, at least one corrosion inhibitor, and optionally effective amounts of fluorometallic compounds such as fluorotitanates, fluorotantalates, fluoroborates, fluorosilicates, divalent zinc compounds, surfactants, wetting agents and/or thickeners.
  • fluorometallic compounds such as fluorotitanates, fluorotantalates, fluoroborates, fluorosilicates, divalent zinc compounds, surfactants, wetting agents and/or thickeners.
  • this invention relates to stable acidic aqueous solutions and the process for treating various metal substrates including pre-coated metal substrates such as anodized aluminum to improve the metal substrates adhesion bonding and corrosion-resistant properties.
  • the process comprises treating the metal substrates with a stable acidic aqueous solution containing effective amounts of at least one water-soluble trivalent chromium salt, at least one water soluble hexafluorozirconate, at least one water soluble poly or mono-carboxylic compound and/or polyhydroxy compound, and at least one water soluble anti-pitting or corrosion inhibitor.
  • compounds that can be added to improve the color and stability of the acidic solutions in small but effective amounts include at least one water soluble hexa or tetra-fluorometallic compounds, divalent zinc salts, and effective amounts of water soluble thickeners and/or water soluble surfactants.
  • This invention comprises a range of aqueous solutions or compositions of specific chemicals and to the processes for depositing coatings derived from these chemicals onto a variety of metallic substrates including pre-existing metal coated substrates.
  • the compositions or solutions are particularly useful for coating aluminum and aluminum alloy i.e.
  • aluminum conversion coatings to enhance corrosion protection and paint adhesion for sealing anodic coatings to enhance corrosion protection; for treatment of titanium or titanium alloys for enhanced paint adhesion; for treatment of magnesium alloys for enhanced paint adhesion and corrosion protection; for coating steel for enhanced paint adhesion and rust inhibition; and for post-treatment of phosphate coatings, zinc, zinc-nickel, tin-zinc, and cadmium sacrificial coatings on iron alloys and other metal substrates e.g. steel for enhanced paint adhesion and corrosion protection.
  • Hexavalent chromium is highly toxic and a known carcinogen. As a result, the solutions used to deposit these coatings and the coatings per se are toxic.
  • the hexavalent chromium films or coatings do, however, yield outstanding paint adhesion, good corrosion resistance, low electrical resistance and can be easily applied by immersion, spray or wipe-on techniques.
  • OSH local occupational, safety, and health
  • hexavalent chromium coatings are becoming more expensive as regulations tighten and costs become prohibitive with future PEL restrictions imposed by the EPA and OSHA.
  • certain processes like spraying chromate solutions are forbidden at some facilities due to OSH risk, forcing the use of less than optimum alternative solutions.
  • hexavalent chromate coatings are technically outstanding, but from a life-cycle cost, environmental, and OSH perspective, alternatives are highly desirable. Accordingly, research is underway to develop alternative processes for metal finishing that are technically equivalent or superior to hexavalent chromate coatings without the environmental and health drawbacks.
  • WO 03/040431 A2 WO 03/040437 A1 and US 6 669 764 B1 are disclosed processes for coating metal substrates to improve corrosion protection and adhesion bonding strength using compositions comprising water-soluble trivalent chromium salts, alkali metal hexafluorozirconat, divalent zinc compounds, surfactants and thickeners.
  • US 4 578 122 discloses a composition containing trivalent chromium for treating metal surfaces to impart a chromium passivate film, wherein carboxylic acids or their salts are used to impart increased clarity and initial hardness to the gelatinous chromate film deposited.
  • This invention relates to compositions as defined in claim 12 and processes for preparing corrosion-resistant coatings on various metallic substrates including pre-coated metal substrates such as phosphate coatings or anodized coatings as defined in claim 1.
  • This invention can be utilized to improve the adhesion of various other coatings such as paint to the metal surface and to prevent pitting and corrosion of the metal surface such as aluminum, steel, galvanized surfaces and the like.
  • the acidic solutions of this invention also contains effective amounts of at least one water-soluble, corrosion-inhibiting or anti-pitting compound together with stabilizing agents consisting of polyhydroxy compounds and/or water-soluble carboxylic compounds containing one or more carboxylic functional groups having the general formula R-COO- wherein R is hydrogen or a lower molecular weight organic radical or functional group.
  • the solution stabilizers i.e. the carboxylic compounds can be used in the form of their acids or salts. In some cases the salts of the carboxylic stabilizers perform better than their acids.
  • organic acids such as formic, acetic, glycolic, propionic, citric and other short-chain or low molecular weight carboxylic acids that naturally buffer in the mildly acidic pH range can be utilized as the solution stabilizers.
  • the advantage of adding the polyhydroxy or carboxylic stabilizers to the acidic solution is the improved shelf-life and working stability of the solutions.
  • the acidic solutions with the addition of the stabilizing agents had substantially no precipitation after more than twenty-four months of shelf-life evaluation and without any degradation of the as-deposited coating performance.
  • Fig's 1-6 show the improved performance of an aluminum alloy coated with the triazole-containing solutions of this invention in comparison to the same coatings without the corrosion-inhibiting triazoles.
  • This invention relates to stable acidic aqueous solutions and to the process of using said aqueous solutions having a pH ranging from about 1.0 to 5.5, and preferably from about 2.5 to 4.5 or 3.4 to 4.0 for preparing zirconium-chromium coatings e.g. a conversion coating on metal substrates including, for example, pre-coated substrates such as anodized aluminum or phosphate coated substrates to improve the adhesion bonding and corrosion-resistance properties of the metal.
  • Phosphate coatings known in the art include, for example, coatings of zinc phosphate, iron phosphate, manganese phosphates and mixed calcium-zinc phosphate coatings.
  • the process comprises using the acidic aqueous solution at temperatures ranging up to about 48.9°C (120°F) or higher e.g. up to about 93.3°C (200°F).
  • the solutions comprise from about 0.01 to 100 grams and preferably from about 0.01 to 22 or 5.0 to 7.0 grams per liter of the acidic solution of at least one water soluble trivalent chromium compound e.g. chromium sulfate, about 0.01 to 24 grams and preferably about 1.0 to 12 or 1.0 to 6.0 grams per liter of the solution of at least one fluorozirconate e.g.
  • an alkali metal salt of H 2 ZrF 6 an effective amount sufficient to inhibit corrosion ranging, for example, from about 0.001 to 4.0 grams per liter and preferably about 0.25 to 2.0 grams or 0.25 to 1.0 gram per liter of a water-soluble corrosion inhibitor or anti-pitting compound such as benzotriazole, and from about 0.001 to 2.0 grams and preferably from 0.001 to 1.0 or 0.01 to 1.0 mole per liter of the solution of at least one water-soluble stabilizing agent or compound selected from the group consisting of carboxylic compounds, polyhydroxy compounds and mixtures of these stabilizing compounds in any ratio. If needed, each of the compounds of this invention can be used up to their solubility limits in the acidic aqueous solutions depending on the metal surface being treated.
  • the metal surfaces treated in accordance with the present invention may be any metal substrate including, for example, iron, zinc, magnesium, steel surfaces including galvanized steel, aluminum and aluminum alloys. Any metal surface, including metal surfaces containing a protective or pre-existing metal coating may be treated with the compositions of the present invention.
  • the coatings are applied after cleaning and deoxidizing or pickling the metal substrate e.g. aluminum substrate via conventional mechanical or chemical techniques.
  • the acidic solution of this invention is applied at about room temperature to the metal substrate via immersion, spray or wipe-on techniques similar to the process used for other metal treatments.
  • Solution dwell time ranges from about 1.0 to 60 minutes or longer. With this solution, the 1.0 to 40 or 1.0 to 10 minute dwell time yields an optimum film for color change, paint adhesion, and corrosion resistance. The 1.0 to 10 minute dwell time yields appreciable color change to the coating depending primarily on the chemical composition of the aqueous solution. The remaining solution is subsequently rinsed from the metal substrate with tap or deionized water.
  • the addition of a thickener to the solution aids in optimum film formation during spray and wipe-on applications by slowing down solution evaporation. This mitigates the formation of powdery deposits that degrade paint adhesion.
  • the addition of thickeners also aids in proper film formation during large area applications and mitigates the diluent effect of rinse water that remains on the substrate during processing from previous steps. This feature of the process yields films or coatings that have no streaks and are an improvement in both coloration and corrosion protection.
  • Water-soluble thickeners such as the cellulose compounds can be present in the acidic aqueous solution in amounts ranging from about 0.0 to 20 grams per liter and preferably 0.5 to 10 grams e.g., about 0.1 to 5.0 grams per liter of the aqueous solution.
  • an effective but small amount of at least one water-soluble surfactant or wetting agent can be added to the acidic solution in amounts ranging from about 0.0 to 20 grams and preferably from 0.5 to 10 grams e.g. 0.1 to 5.0 grams per liter of the acidic solution.
  • the surfactants can be selected from the group consisting of non-ionic, cationic and anionic surfactants.
  • the trivalent chromium is added to the solution as a water-soluble trivalent chromium compound, either as a liquid or solid and preferably as a trivalent chromium salt.
  • the chromium salt can be added conveniently to the solution in its water soluble form wherein the valence of the chromium is plus 3.
  • some of the preferred chromium compounds are incorporated in the solution in the form of Cr 2 (SO 4 ) 3 , (NH 4 )Cr(SO 4 ) 2 , Cr(NO) 3 -9H 2 O or KCr(SO 4 ) 2 and any mixtures of these compounds.
  • a preferred trivalent chromium salt concentration is within the range of about 5.0 to 7.0 grams per liter of the aqueous solution. It has been found that particularly good results are obtained from these processes when the trivalent chromium compound is present in solution in the preferred ranges.
  • the acidic solutions may contain at least one divalent zinc compound to provide color and also improve the corrosion protection of the metal when compared to other treatments or compositions that do not contain zinc.
  • the amount of the zinc compounds can be varied up to the solubility limits to adjust the color imparted to the coating, ranging from 0.0 to 100 grams to as little as about 0.001 grams per liter up to 10 grams per liter e.g. 0.5 to 2.0 grams of Zinc 2 +cation.
  • the divalent zinc can be supplied by any chemical compound e.g. salt that dissolves in water at the required concentration and is compatible with the other components in the acid solution.
  • Divalent zinc compounds that are water soluble at the required concentrations preferably include, for example, zinc acetate, zinc telluride, zinc tetrafluoroborate, zinc molybdate, zinc hexafluorosilicate, zinc sulfate and the like or any combination thereof in any ratio.
  • the treatment or coating of the metal substrates can be carried out at various temperatures including temperatures of the solution which ranges from ambient e.g. from about room temperature up to about 48.9°C (120°F) or higher up to about 93.3°C (200°F). Room temperature is preferred, however, in that this eliminates the necessity for heating equipment.
  • the coating may be air dried by any of the methods known in the art including, for example, oven drying, forced-air drying, exposure to infra-red lamps, and the like.
  • compositions of Examples 1,2 and 3 were used to coat the aluminum alloy (2024-T3) panels as follows:
  • the process comprises cleaning 76 mm by 127 mm by 0.77 mm (3 inch by 5 inch by 0.030 inch) (2024-T3) panels in Turco 425 at 60°C (140°F) for 15 minutes. Rinse in warm tap water using cascading double backflow. Immediately, immerse coupons in Turco Smut Go for 5 minutes. Rinse in ambient temperature tap water using cascading double backflow. Immediately, immerse the panels in the compositions of Examples 1, 2 and 3 for five (5) minutes at 21-27°C (70-80°F). Rinse in ambient temperature tap water using cascading double backflow. Final rinse with deionized water. Let the panels air dry and stand overnight. Coatings are ready for testing or subsequent coating with an organic finish coating e.g. (MIL-PRF-23377) epoxy primer.
  • an organic finish coating e.g. (MIL-PRF-23377) epoxy primer.
  • Test panels were cleaned and coated by the process set forth in Example 7 then placed in neutral salt fog (ASTM B117) at an incline of 6 degrees from vertical. After 3 weeks (21 days) in salt fog, the coating performance is shown in Figures 1-6 .
  • Control coatings were made from the compositions of Examples 1,2 and 3 without the addition of the triazole pitting inhibitors. It is evident from comparing Figures 1-6 (photos) that the addition of the pitting inhibitors resulted in a positive effect on the corrosion resistance of the coatings made from the different compositions.
  • the anti-pitting or corrosion inhibitors are water-soluble compounds selected from the group consisting of triazoles, benzimidazoles, benzazoles, benzoxazoles and mixtures of these inhibitors in any ratio.
  • the preferred corrosion inhibitors or anti-pitting compounds include the triazoles containing up to 12 carbon atoms, such as the alkyl and preferably the aryl triazoles.
  • the aryl triazoles contain from 6-10 carbon atoms, including compounds such as benzotriazole and tolyltriazole, and the alkyl triazoles containing up to six carbons such as methyl or ethyl triazole.
  • the triazoles such as benzotriazole are commercially available under the trade name COBRATEC.
  • the anti-pitting inhibitors are dissolved in the solutions in an effective amount sufficient to inhibit corrosion, and preferably in amounts ranging from about 0.001 to 4.0 grams per liter, and more preferably in amounts of 0.25 to 2.0 grams or from about 0.25 to 1.0 grams per liter.
  • Other useful triazoles include the water soluble hydroxybenzotriazole, such as hydroxy-4-alkylbenzotriazoles, hydroxy-6-benzotriazole, hydroxy-5-chlorobenzotriazole, hydroxy-6-carboxybenzotriazole, hydroxy-5-alkylbenzotriazoles and the like.
  • the stabilizing carboxylic compounds added to the acidic aqueous solutions include water-soluble acids and/or carboxylic acid salts, including the water-soluble carboxylic acids and salts such as adipic, citric, acetic, citraconic, fumaric, glutaric, tartaric acids, or ethylenediamine tetraacetic acid provided the hydrocarbon chain on the carboxylic group does not contain a significant number of carbons which decrease the compounds degree of solubility. Combinations of two or more of the salts and/or acids can be used to obtain a specific pH.
  • the lower molecular acids and/or salts such as potassium formate or citrate can be used at concentrations of at least 0.001 to 2.0 moles or 0.001 to 1.0 mole per liter.
  • These compounds are good all-around stabilizers. Particularly good results were obtained from acidic solutions prepared by adding about 0.01 mole per liter of potassium formate after 4 days of the initial solution preparation. Good results are obtained if the stabilizing agents are carboxylic compounds containing both hydroxy and carboxylic groups including, for example, compounds such as citric acid, glycolic acid, lactic acid, gluconic acids, glutaric acid and their salts.
  • small but effective amount of polyhydroxy compounds also can be used as stabilizers in amounts ranging from about 0.001 to 2.0 and preferably from 0.01 to 2.0 moles or 0.01 to 1.0 mole per liter.
  • the compounds include the trihydric compounds e.g. glycerol and the dihydric ether alcohols e.g. glycol ethers including alkylene glycol ethers, such as triethylene glycol ether, propylene glycol ether, tripropyleneglycol ether, or diethyleneglycol ether.
  • glycols include some of the lower molecular weight compounds such as ethylene glycol, propylene glycol, butylene glycol, cyclohexanol, and the water-soluble poly (oxyalkylene glycols) e.g. the poly-(oxyethylene) or poly-(oxypropylene glycols), having lower molecular weights ranging up to about 1000 may be employed to promote stability and dispersibility of solids in the coating bath or acid solutions.
  • di- and trihydric aliphatic alcohols include the water soluble lower alkanols, such as the di- and tri-hydric alkanols containing up to twelve carbon atoms.
  • This class of di- and trihydric lower alkanols can include glycols containing up to ten carbon atoms in the alkylene group e.g. trimethylene glycol, and the polyglycols, such as diethylene glycol, triethylene glycol, tetraethylene glycol, dipropylene glycol, tripropylene glycol, dibutylene glycol, tributylene glycol, and other polyalkylene glycols wherein the alkylene radical contains up to eight carbon atoms and preferably from two to four carbon atoms. Combinations or mixtures of the carboxylic and polyhydroxy stabilizing compounds may be used in the acidic solution in any ratio.
  • the acidic aqueous solutions may contain small but effective amounts of from 0.0 to 24 grams e.g. 0.01 to 12 grams per liter of solution of at least one fluorometallic compound preferably including stabilizing compounds such as hexafluorotitanate, heptafluorotantalate, tetrafluoroborate and hexafluorosilicate.
  • known water soluble surfactants can be added to the trivalent chromium solutions in amounts ranging from about 0 to 20 grams per liter and preferably about 5.0 to 10 grams or 1.0 to 5.0 grams per liter.
  • the surfactants are added to the aqueous solution to provide better wetting properties by lowering the surface tension thereby insuring complete coverage, and a more uniform film on the metal substrates.
  • the surfactants include at least one water soluble compound selected from the group consisting of non-ionic, anionic, and cationic surfactants.
  • Some of the better known water soluble surfactants include the monocarboxyl imidoazoline, alkylsulfate sodium salts (DUPONOL®), ethoxylated or propoxylated alkylphenol (IGEPAL®), alkylsulfonamides, alkaryl sulfonates, palmiticalkanol amides (CENTROL®), octylphenyl polyethoxy ethanol (TRITON®), sorbitan monopalmitate (SPAN®); dodecylphenyl polyethyleneglycol ether (TERGITROL®), alkyl pyrrolidones, polyalkoxylated fatty acid esters, alkylbenzene sulfonates and mixtures thereof.
  • DUPONOL® alkylsulfate sodium salts
  • IGEPAL® ethoxylated or propoxylated alkylphenol
  • alkylsulfonamides alkaryl sulfonates
  • water soluble surfactants include, for example, the nonylphenol ethoxylates, and adducts of ethylene oxide with fatty amines; see the publication: “Surfactants and Detersive Systems", by John Wiley et al. in Kirk-Othmer's Encyclopedia of Chemical Technology, 3 rd Ed.
  • thickening agents can be added to retain the aqueous solution on the surface for sufficient contact time.
  • the thickeners employed are known inorganic and preferably the organic water soluble thickeners added to the trivalent chromium solutions in effective amounts e.g. at sufficient concentrations ranging from about 0 to 20 grams per liter and preferably 0.5 to 10 grams or 1.0 to 5.0 grams per liter of the acidic solution.
  • Specific examples of some preferred thickeners include the cellulose compounds, e.g. hydroxypropyl cellulose (Klucel), ethyl cellulose, hydroxyethyl cellulose, hydroxymethyl cellulose, methyl cellulose and mixtures thereof.
  • Other water soluble inorganic thickeners include colloidal silica, clays such as bentonite, starches, gum arabic, tragacanth, agar and various combinations.
  • the solution can be applied via immersion, spray or wipe-on techniques.
  • the TCP solutions of this invention can be used at elevated temperatures ranging up to 48.9°C (120°F) or higher e.g. up to 93.3°C (200°F) and optimally applied via immersion to further improve the corrosion resistance of the coatings.
  • Solution dwell time ranges from about 1 to 60 minutes, and preferably 1.0 to 40 or 1.0 to 10 minutes at about 23.9°C (75°F) or higher. After dwelling, the remaining solution is then thoroughly rinsed from the substrate with tap or deionized water. No additional chemical manipulations of the deposited films are necessary for excellent performance.
  • the aqueous solutions may be sprayed from a spray tank apparatus designed to replace immersion tanks.

Claims (29)

  1. Procédé de revêtement de substrats métalliques pour améliorer la protection contre la corrosion et la résistance de liaison par adhérence du métal, qui comprend le traitement des substrats métalliques avec une solution aqueuse acide ayant, un pH de l'ordre de 1,0 à 5,5 ; ladite solution aqueuse acide comprenant par litre de solution, de 0,01 à 100 grammes d'au moins un composé de chrome trivalent, de 0,01 à 24 grammes d'au moins un fluorozirconate, de 0,0 à 100 grammes de composés de zinc divalents, de 0,0 à 20 grammes de tensioactifs, de 0,0 à 20 grammes d'épaississants,
    caractérisé en ce que
    ladite solution acide comprend en outre 0,001 à 4,0 grammes par litre d'au moins un inhibiteur de corrosion hydrosoluble choisi dans le groupe comprenant des triazoles, des benzimidazoles, des benzazoles et des benzoxazoles, et 0,001 à 2,0 grammes par litre d'un composé stabilisant choisi dans le groupe comprenant des composés polyhydroxy, des composés carboxyliques et des mélanges de composés polyhydroxy et carboxyliques, lesdits' composés polyhydroxy étant choisis dans le groupe comprenant le glycérol, l'éther de méthylène glycol, l'éther de propylène glycol, l'éther de tripropylène glycol, l'éther de diéthylène glycol, le glycol, le propylène glycol, le butylène glycol, le cyclohexanol, les poly(oxyéthylène glycols) hydrosolubles et les poly(oxypropylène glycols) ayant des poids moléculaire allant jusqu'à environ 1000, le triméthylène glycol, le diéthylène glycol, le méthylène glycol, le tétraéthylène glycol, le dipropylène glycol, le tripropylène glycol, le dibutylène glycol, le tributylène glycol et les polyalkylène glycols, le radical alkylène contenant jusqu'à huit atomes de carbone et lesdits composés carboxyliques étant choisis dans le groupe comprenant les acides formique, acétique, propionique, citrique, adipique, citraconique, fumarique, glutarique, tartrique, lactique, glycolique, gluconique et éthylène diamine tétra-acétique et leurs sels.
  2. Procédé selon la revendication 1, dans lequel les substrats métalliques ont un revêtement métallique préexistant sur ceux-ci.
  3. Procédé selon la revendication 2, dans lequel le substrat revêtu de métal préexistant est au moins un substrat parmi un revêtement d'aluminium anodisé et un revêtement de phosphate.
  4. Procédé selon la revendication 1, dans lequel le substrat métallique est au moins un substrat parmi un alliage d'aluminium et un alliage de fer.
  5. Procédé selon la revendication 1, dans lequel le composé carboxylique est au moins un composé parmi un composé hydroxy-carboxylique, un acide formique, un acide propionique et les sels hydrosolubles de ceux-ci.
  6. Procédé selon la revendication 1, dans lequel l'inhibiteur de corrosion hydrosoluble est le benzotriazole.
  7. Procédé selon la revendication 5, dans lequel le composé hydroxy-carboxylique est au moins un composé parmi un acide citrique, un acide gluconique, un acide glycolique et les sels hydrosolubles de ceux-ci.
  8. Procédé selon la revendication 1, dans lequel la solution aqueuse acide contient de 0,001 à 1,0 mole par litre de composé carboxylique et l'inhibiteur est un triazole.
  9. Procédé selon la revendication 1, dans lequel la solution aqueuse acide contient de 0,001 à 2,0 moles par litre de composé stabilisant et 0,025 à 4,0 grammes par litre d'un triazole.
  10. Procédé selon la revendication 1, dans lequel le composé stabilisant est le glycérol et l'inhibiteur de corrosion hydrosoluble est un mélange de benzotriazole et de tolyltriazole.
  11. Procédé selon la revendication 1, dans lequel le composé stabilisant est un composé carboxylique ayant plus d'un groupe carboxylique fonctionnel par molécule.
  12. Compositions de revêtement de substrats métalliques pour améliorer la protection contre la corrosion et la résistance de liaison par adhérence dudit métal, qui comprennent une solution aqueuse acide ayant un pH de l'ordre de 1,0 à 5,5 et par litre de ladite solution, de 0,01 à 100 grammes d'au moins un composé de chrome trivalent, de 0,01 à 24 grammes d'au moins un fluorozirconate, de 0,0 à 20 grammes de composés de zinc divalents, de 0,0 à 20 grammes de tensioactifs, de 0,0 à 20 grammes d'épaississants,
    caractérisées en ce que
    ladite solution aqueuse acide comprend en outre de 0,001 à 4,0 grammes par litre d'au moins un inhibiteur de corrosion hydrosoluble choisi dans le groupe comprenant des triazoles, des benzimidazoles, des benzazoles et des benzoxazoles et des mélanges desdits inhibiteurs, et de 0,001 à 2,0 grammes par litre d'un composé stabilisant choisi dans le groupe comprenant des composés polyhydroxy, des composés carboxyliques et des mélanges de composés polyhydroxy et carboxyliques, lesdits composés polyhydroxy étant choisis dans le groupe comprenant le glycérol, l'éther de méthylène glycol, l'éther de propylène glycol, l'éther de tripropylène glycol, l'éther de diéthylène glycol, le glycol, le propylène glycol, le butylène glycol, le cyclohexanol, les poly(oxyéthylène glycols) hydrosolubles et les poly(oxypropylène glycols) ayant des poids moléculaire allant jusqu'à environ 1000, le triméthylène glycol, le diéthylène glycol, le méthylène glycol, le tétraéthylène glycol, le dipropylène glycol, le tripropylène glycol, le dibutylène glycol, le tributylène glycol et les polyalkylène glycols, le radical alkylène contenant jusqu'à huit atomes de carbone et lesdits composés carboxyliques étant choisis dans le groupe comprenant les acides formique, acétique, propionique, citrique, adipique, citraconique, fumarique, glutarique, tartrique, lactique, glycolique, gluconique et éthylène diamine tétra-acétique et leurs sels.
  13. Composition selon la revendication 12, dans laquelle le composé stabilisant est un composé carboxylique ayant plus d'un groupe carboxylique fonctionnel par molécule.
  14. Composition selon la revendication 13, dans laquelle le composé carboxylique est un acide hydroxy-carboxylique et les sels hydrosolubles de celui-ci.
  15. Composition selon la revendication 14, dans laquelle le composé hydroxy-carboxylique est choisi dans le groupe comprenant l'acide citrique, l'acide glycolique, l'acide lactique, les sels hydrosolubles de ceux-ci et leurs combinaisons.
  16. Composition selon la revendication 12, dans laquelle le composé carboxylique est au moins un composé parmi un acide formique, un acide propionique et les sels hydrosolubles de ceux-ci.
  17. Composition selon la revendication 12, dans laquelle le composé polyhydroxy est le glycérol, le composé carboxylique est un acide carboxylique de poids moléculaire inférieur ou un sel hydrosoluble de celui-ci et l'inhibiteur de corrosion hydrosoluble est un triazole.
  18. Composition selon la revendication 12, dans laquelle le composé stabilisant est un mélange d'un acide carboxylique à poids moléculaire inférieur et d'un composé polyhydroxy.
  19. Composition selon la revendication 12, dans laquelle le composé stabilisant est un composé polyhydroxy de bas poids moléculaire et l'inhibiteur de corrosion hydrosoluble est le mercaptobenzimidazole.
  20. Composition selon la revendication 12, dans laquelle le composé polyhydroxy est le glycérol et l'inhibiteur de corrosion hydrosoluble est au moins un benzotriazole et un mélange de triazoles.
  21. Composition selon la revendication 12, dans laquelle le composé de zinc divalent est un sel de zinc hydrosoluble présent dans la solution aqueuse acide en une quantité allant de 0,5 à 2,0 grammes et l'inhibiteur de corrosion hydrosoluble est au moins un inhibiteur parmi un benzotriazole et un mercaptobenzazole.
  22. Composition selon la revendication 12, dans laquelle le composé polyhydroxy est un polyalkylène glycol et l'inhibiteur de corrosion hydrosoluble est le benzimidazole.
  23. Composition selon la revendication 12, dans laquelle le pH va de 2,5 à 4,5, le composé de chrome trivalent va de 0,01 à 22 grammes, le fluorozirconate est un hexafluorozirconate allant de 1,0 à 12 grammes, les composés stabilisants vont de 0,001 à 1,0 mole par litre et l'inhibiteur est un triazole allant de 0,001 à 4,0 grammes par litre de solution.
  24. Composition selon la revendication 23, dans laquelle le composé stabilisant est un acide carboxylique de poids moléculaire inférieur ou un sel hydrosoluble de celui-ci et le triazole est le tolyltriazole.
  25. Composition selon la revendication 12, dans laquelle le composé stabilisant est un composé polyhydroxy et l'inhibiteur de corrosion hydrosoluble est le mercaptobenzazole.
  26. Composition selon la revendication 12, dans laquelle le composé de zinc divalent va de 0,001 à 10 grammes et l'inhibiteur de corrosion hydrosoluble est un benzazole.
  27. Composition selon la revendication 12, dans laquelle les épaississants et/ou les tensioactifs vont de 1,0 à 5,0 grammes et l'inhibiteur de corrosion hydrosoluble est le mercaptobenzazole.
  28. Composition selon la revendication 12, dans laquelle la solution aqueuse acide contient de 0,01 à 12 grammes par litre d'au moins un composé fluorométallique choisi dans le groupe comprenant les fluorotitanates, les fluorotantalates, les fluoroborates, les fluorosilicates et leurs mélanges et l'inhibiteur de corrosion hydrosoluble est un mélange desdits inhibiteurs.
  29. Composition selon la revendication 28, dans laquelle le composé fluorométallique est au moins un composé parmi un hexafluorosilicate et un tétrafluoroborate, le fluorozirconate est un hexafluorozirconate et l'inhibiteur de corrosion hydrosoluble est au moins un inhibiteur parmi un tolyltriazole et un benzotriazole.
EP05851727A 2005-02-15 2005-11-14 Composition et procede de preparation de revetements de protection sur des substrats metalliques Active EP1863952B1 (fr)

Applications Claiming Priority (5)

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US11/076,106 US20060180247A1 (en) 2005-02-15 2005-02-15 Process for preparing chromium conversion coatings for iron and iron alloys
US11/058,715 US20100032060A1 (en) 2005-02-15 2005-02-15 Process for preparing chromium conversion coatings for magnesium alloys
US11/116,165 US7811391B2 (en) 2005-04-21 2005-04-21 Composition and process for preparing protective coatings on metal substrates
US11/116,166 US20060240191A1 (en) 2005-04-21 2005-04-21 Composition and process for preparing chromium-zirconium coatings on metal substrates
PCT/US2005/041587 WO2006088521A2 (fr) 2005-02-15 2005-11-14 Composition et procede de preparation de revetements de protection sur des substrats metalliques

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Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102066611B (zh) * 2008-04-25 2013-09-18 汉高股份及两合公司 用于处理镀锌钢的三价铬钝化剂
US8591670B2 (en) 2008-05-07 2013-11-26 Bulk Chemicals, Inc. Process and composition for treating metal surfaces using trivalent chromium compounds
DE102009028025A1 (de) 2009-07-27 2011-02-03 Henkel Ag & Co. Kgaa Mehrstufiges Verfahren zur Behandlung von Metalloberflächen vor einer Tauchlackierung
EP2711444A1 (fr) 2012-09-20 2014-03-26 Coventya SAS Solution aqueuse alcaline pour améliorer la résistance à la corrosion d'un revêtement de conversion Cr(III), procédé de production d'un tel revêtement et son utilisation
US10156016B2 (en) * 2013-03-15 2018-12-18 Henkel Ag & Co. Kgaa Trivalent chromium-containing composition for aluminum and aluminum alloys
JP6545191B2 (ja) * 2014-12-26 2019-07-17 ディップソール株式会社 亜鉛又は亜鉛合金基材用3価クロム化成処理液及び化成皮膜
US10435806B2 (en) 2015-10-12 2019-10-08 Prc-Desoto International, Inc. Methods for electrolytically depositing pretreatment compositions
JP7399080B2 (ja) 2017-05-12 2023-12-15 ケメオン サーフェス テクノロジー, エルエルシー pH安定な三価クロムコーティング液
CA3089314A1 (fr) * 2018-01-30 2019-08-08 Prc-Desoto International, Inc. Systemes et procedes de traitement d'un substrat metallique
JP7118402B2 (ja) * 2018-04-26 2022-08-16 奥野製薬工業株式会社 アルミニウム合金の陽極酸化皮膜用封孔処理液、濃縮液及び封孔処理方法
CN113272400A (zh) * 2019-02-21 2021-08-17 Mec股份有限公司 接着组合物、表面处理金属构件的制造方法、及金属-树脂复合体的制造方法
AU2022376938A1 (en) * 2021-10-27 2024-05-02 Prc-Desoto International, Inc. Compositions, systems and methods for treating a substrate

Family Cites Families (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4578122A (en) * 1984-11-14 1986-03-25 Omi International Corporation Non-peroxide trivalent chromium passivate composition and process
DE3521952A1 (de) * 1985-06-20 1987-01-02 Henkel Kgaa Waessrige zusammensetzungen fuer den hilite- und flux-prozess und ihre verwendung
DE3783173T2 (de) * 1986-07-23 1993-04-22 Fuji Photo Film Co Ltd Verfahren zur behandlung eines farbphotographischen silberhalogenidmaterials und farbentwickler.
JPH0225592A (ja) * 1988-07-14 1990-01-29 Fujitsu Ltd 陽極酸化皮膜の封孔処理方法
JPH07100873B2 (ja) * 1989-09-27 1995-11-01 日本パーカライジング株式会社 亜鉛系メッキ鋼板のクロメート塗布液
US5226976A (en) * 1991-04-15 1993-07-13 Henkel Corporation Metal treatment
DE19615664A1 (de) * 1996-04-19 1997-10-23 Surtec Produkte Und Systeme Fu Chrom(VI)freie Chromatschicht sowie Verfahren zu ihrer Herstellung
CA2271730A1 (fr) * 1996-11-27 1998-06-04 Henkel Corporation Composition aqueuse et procede de preparation d'un substrat metallique destine a un formage a froid
JP3391252B2 (ja) * 1998-03-26 2003-03-31 日本軽金属株式会社 電着塗装アルミ材の製造方法
JP2002075767A (ja) * 2000-08-31 2002-03-15 Sumitomo Special Metals Co Ltd 耐食性被膜を有する希土類系永久磁石およびその製造方法
WO2002031222A2 (fr) * 2000-10-11 2002-04-18 Chemetall Gmbh Procede pour enduire des surfaces metalliques avec une composition aqueuse, composition aqueuse et utilisation des substrats ainsi revetus
US6669764B1 (en) * 2000-10-31 2003-12-30 The United States Of America As Represented By The Secretary Of The Navy Pretreatment for aluminum and aluminum alloys
US6527841B2 (en) * 2000-10-31 2003-03-04 The United States Of America As Represented By The Secretary Of The Navy Post-treatment for metal coated substrates
US6663700B1 (en) * 2000-10-31 2003-12-16 The United States Of America As Represented By The Secretary Of The Navy Post-treatment for metal coated substrates
US6511532B2 (en) * 2000-10-31 2003-01-28 The United States Of America As Represented By The Secretary Of The Navy Post-treatment for anodized aluminum
JP2002212746A (ja) * 2001-01-11 2002-07-31 Okuno Chem Ind Co Ltd 未貫通穴を有する被めっき物への無電解ニッケルめっき方法
WO2003060019A1 (fr) * 2002-01-04 2003-07-24 University Of Dayton Pigments anticorrosion non toxiques a base de cobalt
JP3774415B2 (ja) * 2002-03-14 2006-05-17 ディップソール株式会社 亜鉛及び亜鉛合金めっき上に黒色の六価クロムフリー化成皮膜を形成するための処理溶液及び亜鉛及び亜鉛合金めっき上に黒色の六価クロムフリー化成皮膜を形成する方法。
JP2003306756A (ja) * 2002-04-18 2003-10-31 Jfe Steel Kk 溶融亜鉛めっき鋼板とその製造方法
JP2004083771A (ja) * 2002-08-28 2004-03-18 Nippon Hyomen Kagaku Kk 金属保護被膜形成用組成物
DE10310972A1 (de) * 2003-03-13 2004-09-23 Basf Ag Stickstoffhaltige Polymere für die Metalloberflächenbehandlung

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JP5060964B2 (ja) 2012-10-31
CA2597630A1 (fr) 2006-08-24
AU2005327548A1 (en) 2006-08-24
WO2006088521A2 (fr) 2006-08-24
BRPI0519981B1 (pt) 2016-03-08
BRPI0519981A2 (pt) 2009-08-18
JP2008537975A (ja) 2008-10-02
KR20080000564A (ko) 2008-01-02
CA2597630C (fr) 2015-09-29
DK1863952T3 (da) 2013-03-25
ES2411429T3 (es) 2013-07-05
MX2007009801A (es) 2007-10-03
EP1863952A2 (fr) 2007-12-12
EP1863952A4 (fr) 2010-01-13

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