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EP3856947B1 - Method for improving the phosphatability of metal surfaces which are provided with a temporary pre- or post-treatment - Google Patents

Method for improving the phosphatability of metal surfaces which are provided with a temporary pre- or post-treatment Download PDF

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Publication number
EP3856947B1
EP3856947B1 EP19778901.9A EP19778901A EP3856947B1 EP 3856947 B1 EP3856947 B1 EP 3856947B1 EP 19778901 A EP19778901 A EP 19778901A EP 3856947 B1 EP3856947 B1 EP 3856947B1
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EP
European Patent Office
Prior art keywords
coating
zinc
steel product
flat steel
activation particles
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.)
Active
Application number
EP19778901.9A
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German (de)
French (fr)
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EP3856947A1 (en
Inventor
Fabian JUNGE
Christian Altgassen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ThyssenKrupp Steel Europe AG
ThyssenKrupp AG
Original Assignee
ThyssenKrupp Steel Europe AG
ThyssenKrupp AG
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Publication of EP3856947A1 publication Critical patent/EP3856947A1/en
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/26After-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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/04Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the coating material
    • C23C2/06Zinc or cadmium or alloys based thereon
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/18Orthophosphates containing manganese cations
    • C23C22/182Orthophosphates containing manganese cations containing also zinc cations
    • C23C22/184Orthophosphates containing manganese cations containing also zinc cations containing also nickel cations
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/73Chemical 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
    • 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
    • C23C22/78Pretreatment of the material to be coated
    • 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
    • C23C22/78Pretreatment of the material to be coated
    • C23C22/80Pretreatment of the material to be coated with solutions containing titanium or zirconium compounds
    • 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
    • C23C2222/20Use of solutions containing silanes

Definitions

  • the present invention relates to a method for producing a formed component, comprising at least the steps (A) providing a flat steel product, (B) skin rolling the flat steel product from step (A), (C) applying a functional coating to the flat steel product from step (B), (D) forming the flat steel product from step (C) to obtain a formed component, (E) removing the functional coating from the formed component from step (D), (F) applying activation particles to the formed component from step (E), and (G) applying a phosphating to the formed component from step (F), wherein additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C). Furthermore, the present invention relates to a corresponding flat steel product and its use in the automotive sector.
  • US 2015/0352825 A1 discloses a process in which a flat steel product having an anti-corrosive coating is first treated with an acidic solution so that a subsequently applied adhesive shows better adhesion.
  • WO 2017/125131 A1 discloses a method for producing a steel product having a zinc-based protective coating and a tribologically active layer applied to the protective coating.
  • the anti-corrosive coated steel flat products known from the state of the art often have the problem that during their production a temporary pre- or post-treatment, i.e. a functional coating such as an adhesion-promoting layer, a forming aid, a passivation or a combination thereof, is applied and then removed again. This removal is usually carried out by a cleaning step. It can happen that the cleaning step is not completed, i.e. that residues of the functional coating remain on at least some areas of the flat steel product.
  • a temporary pre- or post-treatment i.e. a functional coating such as an adhesion-promoting layer, a forming aid, a passivation or a combination thereof
  • a subsequent two-stage phosphating step which includes the application of activation particles and phosphating, the activation particles cannot fully reach the actual surface of the flat steel product due to the residues of the functional layer, so that the result is a phosphate layer that consists in areas of zinc phosphate crystals of different sizes that appear uneven when viewed macroscopically, which is undesirable.
  • the object of the present invention is therefore to provide a method for producing a phosphated flat steel product which, compared to the prior art, produces improved phosphated surfaces which, in particular, exhibit better adhesive adhesion.
  • the invention aims to provide a method which produces good phosphated surfaces, in particular with improved adhesive adhesion, even when functional coatings applied in the meantime have not been completely removed.
  • Step (A) of the method according to the invention comprises providing a flat steel product.
  • a flat steel product provided with a coating that protects against corrosion is provided.
  • the flat steel product used according to the invention can consist of any steel grade known to the person skilled in the art, for example CR3 or DX51.
  • This steel preferably used according to the invention contains, for example, max. 0.08 wt.% C, max. 0.45 wt.% Mn, max. 0.030 wt.% P, max. 0.030 wt.% S, max. 0.15 wt.% Cr, max. 0.20 wt.% Cu, max. 0.06 wt.% Mo, max. 0.008 wt.% Nb, max. 0.20 wt.% Ni, where the sum of Cu, Ni, Cr and Mo must not exceed 0.50 wt.% and the sum of Cr and Mo must not exceed 0.16 wt.%, the remainder being Fe and unavoidable impurities.
  • the flat steel product according to the invention is a hot strip or a cold strip. These can be obtained by methods known to those skilled in the art.
  • so-called blanks can also be used in step (A) of the method according to the invention, which are preferably obtained by cutting pieces from a hot or cold strip using suitable methods.
  • the flat steel product according to the invention is based on a steel sheet, preferably containing a coating that protects against corrosion.
  • the coating that protects against corrosion which is preferably present according to the invention, is preferably metallic.
  • the steel sheet can be coated in a known manner, for example in a hot-dip process (hot-dip galvanizing) or by electrolytic deposition. According to the invention, the coating is preferably carried out in a hot-dip process. Corresponding processes are known per se to those skilled in the art.
  • the coating that is preferably present on the flat steel product according to the invention is preferably based on zinc, a zinc alloy, aluminum or an aluminum alloy.
  • a non-coated, in particular non-galvanized, steel surface can also be used in step (A).
  • Suitable coatings therefore contain, for example, zinc or zinc and magnesium, zinc and aluminium or zinc which has been applied electrolytically.
  • the flat steel product in particular the steel strip, is preferably coated by first mechanically and/or chemically cleaning the strip surface in a first stage of the coating process.
  • the strip surface is then roughened, preferably in an acidic pickling solution, before the strip is passed through an electrolytic coating cell and coated, in particular galvanized, there.
  • the steel strip is dipped in a sulfuric acid zinc electrolyte and simultaneously switched as a cathode.
  • soluble electrodes these are also dipped in the electrolyte solution and switched as an anode.
  • the cations migrate from the anode through the electrolyte to the steel strip surface and are cathodically deposited there.
  • the metal for example zinc
  • the electrolyte is already dissolved in the electrolyte, whereby the anodes consist of correspondingly more noble materials.
  • the amount of metal deposited on the strip surface depends on the current density and the coating duration.
  • the steel strip In order to achieve a metal layer thickness of a few micrometers at a belt speed of, for example, 100 m/min, the steel strip must pass through several coating cells connected in series in an electrolytic cell because of the relatively short coating time and thus the correspondingly low deposition rate at such a belt speed.
  • the electrolytically coated steel strip is preferably passed through a multi-stage rinsing device.
  • the present coating particularly preferably consists of zinc or a zinc alloy, which has more preferably been applied by hot-dip coating.
  • Methods for hot-dip coating are known per se to those skilled in the art.
  • the coating in particular made of zinc or a zinc alloy, is preferably present with a coating weight of 1 to 600 g/m 2 , ie 0.5 to 300 g/m 2 per side, particularly preferably 20 to 300 g/m 2 , ie 10 to 150 g/m 2 per side.
  • Step (B) of the process according to the invention comprises the skin passing of the flat steel product from step (A).
  • Dressing is known to the expert and is described, for example, in Handbook of forming, Günter Spur, ISBN: 978-3-446-43004-4, page 155 .
  • the present invention preferably relates to the method according to the invention, wherein the skin-passing in step (B) is carried out using a skin-passing agent.
  • a skin-passing agent is therefore applied to the flat steel product before and/or during step (B).
  • Usable skin-passing agents are known per se to the person skilled in the art.
  • the at least one dressing agent contains organic compounds selected from the group consisting of saturated hydrocarbons, in particular hydrogenated naphtha, alkoxylated alcohols, in particular 2-(2-butoxyethoxy)ethanol, 2-(methoxymethyloxy)propane and/or branched poly(oxy-1,2-ethanediyl)-alpha-tridecyl-omega-alcohol, adducts of organic acids and amines, for example the adduct of 3,5,5-trimethylhexanoic acid and 2-aminoethanol, derivatives of fatty acids, for example oleoylsarcosine, amines, for example dodecylpropylenetriamine, glycols, for example hexylene glycol, and mixtures thereof.
  • saturated hydrocarbons in particular hydrogenated naphtha
  • alkoxylated alcohols in particular 2-(2-butoxyethoxy)ethanol, 2-(methoxymethyloxy)propane and/or branched poly(oxy-1
  • the at least one dressing agent is selected from the group consisting of compositions with the trade names Friocut LF 280, Gardolube L 8256, QWERL 4305 and mixtures thereof.
  • the present invention therefore preferably relates to the process according to the invention, wherein at least one skin-pass agent and additional activation particles are applied to the flat steel product before and/or during step (B).
  • a mixture containing at least one skin-pass agent and additional activation particles is applied to the flat steel product before and/or during step (B).
  • At least one skin-pass agent and additional activation particles are applied separately to the flat steel product before and/or during step (B).
  • the at least one skin-pass agent is generally applied to the flat steel product in an amount such that the subsequent skin-pass step can proceed advantageously.
  • the at least one skin-pass agent is applied in an amount of 1 to 50 g/L, particularly preferably 10 to 30 g/L.
  • the application of the at least one dressing agent and optionally the activation particles can generally be carried out by all methods known to the person skilled in the art, for example spraying, dipping or coating methods.
  • Step (C) of the process according to the invention comprises applying a functional coating to the flat steel product from step (B).
  • the steel product obtained after the skin passing in step (B) contains on the surface at least parts of the possibly applied skin passing agent and, if applicable, additional activation particles.
  • step (C) of the method according to the invention at least one functional coating is applied to this flat steel product.
  • Functional coatings are also known to the person skilled in the art under the term "pre- or post-treatments”.
  • Functional coatings that can be applied to the flat steel product in the method according to the invention are known to the person skilled in the art and are selected, for example, from the group consisting of adhesion-promoting layer, forming aid, passivation or a combination thereof.
  • Suitable adhesion-promoting coatings are known to the person skilled in the art and contain, for example, alcohols, for example methanol, silane components, for example Polysiloxanes, silicate components, ammonium or amino compounds, organic polymers and mixtures thereof.
  • the at least one adhesion promoter is selected from the group consisting of compositions with the trade names GBX 4537, Bonderite 1461 and mixtures thereof.
  • An adhesion-promoting layer can be applied to the flat steel product by any method known to the person skilled in the art, for example spraying, dipping or coating processes.
  • An adhesion-promoting coating is generally applied in an amount sufficient to exert the adhesion-promoting effect, for example 1 mg/m 2 to 10 mg/m 2 , preferably 2 mg/m 2 to 6 mg/m 2 , in each case per layer of the silicon conductive element.
  • Suitable coatings that can act as a forming aid are known per se to the person skilled in the art and contain, for example, acids, for example phosphoric acid, bases, for example potassium hydroxide or organic amines, cyclic organic compounds, for example benzotriazole, other organic compounds, for example fatty acids, sulfonates, for example methanesulfonate, or alcohols, for example aminoethanol, inorganic salts, for example sulfates, in particular zinc sulfate or potassium sulfate, or carbonates, for example sodium carbonate, preferably as aqueous solutions.
  • acids for example phosphoric acid
  • bases for example potassium hydroxide or organic amines
  • cyclic organic compounds for example benzotriazole
  • other organic compounds for example fatty acids, sulfonates, for example methanesulfonate, or alcohols, for example aminoethanol
  • inorganic salts for example sulfates, in particular zinc sulfate or potassium s
  • the at least one forming aid is selected from the group consisting of compositions with the trade names Lubitreat, NIT, L-FM50000, L-FM50100, L-FM50200 and mixtures thereof.
  • a coating acting as a forming aid can be applied to the flat steel product by any method known to the person skilled in the art, for example spraying, dipping or coating processes.
  • a coating acting as a forming aid is generally applied in an amount sufficient to produce the corresponding effect, for example 5 mg/m 2 to 40 mg/m 2 , preferably 10 mg/m 2 to 25 mg/m 2 , in each case based on the sulfur conductive element.
  • Suitable passivating coatings are known per se to the person skilled in the art and contain, for example, chromium salts, for example chromium orthophosphate, chromium nitrate, chromium trifluoride, organic acids, for example citric acid, inorganic acids, for example hydrofluoric acid, and mixtures thereof.
  • the at least one passivating agent is selected from the group consisting of compositions with the trade names Gardolene D 6804, Gardolene D 6811, Bonderite M-PA 6003 and mixtures thereof.
  • a passivating coating can be applied to the flat steel product by any method known to the person skilled in the art, for example spraying, dipping or coating processes.
  • a passivating coating is generally applied in an amount sufficient to exert the passivating effect, for example 5 mg/m 2 to 40 mg/m 2 , preferably 10 mg/m 2 to 25 mg/m 2 , in each case based on the conductive element chromium, in the case of chromium-containing passivations.
  • step (C) of the process according to the invention two or more of the coatings mentioned are applied in appropriate amounts. This can be done sequentially or simultaneously.
  • the present invention preferably relates to the process according to the invention, wherein at least one functional coating agent and additional activation particles are applied before and/or during step (C).
  • a mixture containing at least one functional coating agent and additional activation particles is applied to the flat steel product before and/or during step (C).
  • At least one functional coating agent and additional activation particles are applied separately to the flat steel product before and/or during step (C).
  • Step (D) of the method according to the invention comprises forming the flat steel product from step (C) in order to obtain a formed component.
  • blanks are preferably first cut from the hot strip or cold strip at the beginning of step (D). This can be done using methods known to those skilled in the art.
  • the forming of the flat steel product from step (C) can be carried out by all methods known to the person skilled in the art, for example according to DIN 8580 (2010) and in particular DIN 8584 (2010).
  • the transformation preferably takes place at room temperature.
  • Step (E) of the method according to the invention comprises removing the functional coating from the formed component from step (D).
  • Step (E) of the process according to the invention can generally be carried out by any method known to the person skilled in the art, for example described in EP 2 311 928 A2 , EP 2 851 452 A1 and EP 2 937 411 A1 .
  • step (E) of the method according to the invention is carried out in that the formed component from step (D) can be treated with at least one cleaning agent in order to remove the functional coating.
  • the functional coating is removed in step (E) of the method according to the invention by treating the surface of the formed component with a cleaning agent.
  • the cleaning agent can be acidic, neutral or alkaline.
  • an alkaline cleaning agent is used.
  • the cleaning agent is also preferably used as an aqueous solution.
  • the cleaning-active substance for example a surfactant, is preferably present in an amount that appears suitable to the person skilled in the art.
  • Further components of the cleaning agent which are preferably present according to the invention are, for example, selected from the group consisting of sodium hydroxide or potassium hydroxide and mixtures thereof.
  • Step (E) of the method according to the invention can also be carried out using mechanical energy, for example by brushing the surfaces to be cleaned or by applying water and/or cleaning agents to the surface under high pressure.
  • Step (E) of the method according to the invention is preferably carried out at a temperature of 30 to 70 °C.
  • the cleaning in step (E) of the method according to the invention is complete, since the best result is then achieved in the phosphating in step (G).
  • the cleaning in step (E) of the method according to the invention does not necessarily have to be complete in order to obtain a particularly advantageous result in the phosphating step.
  • by applying additional activation particles to the flat steel product before and/or during step (B) and/or before and/or during step (C) it is possible to obtain a very good phosphating result, even though the functional coating does not have to have been completely removed. This circumstance greatly simplifies the process and helps to obtain high-quality phosphated and formed components.
  • the method according to the invention therefore comprises the feature essential to the invention that additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C).
  • the additional activation particles may differ from the activation particles used in step (F).
  • the additional activation particles and the activation particles used in step (F) of the process according to the invention are the same.
  • the additional activation particles are preferably selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides.
  • water-dispersible compounds are used, for example oxalates of silver or copper compounds, disodium phosphate in combination with titanium compounds, in particular with water-soluble titanium compounds, for example titanium phosphate or sodium titanyl phosphates, zinc phosphates and mixtures of zinc phosphates and metal oxides, e.g. zinc or iron oxides and mixtures thereof.
  • the additional activation particles are preferably applied in powder form or as an aqueous composition.
  • the batch concentration of the activating agent is, for example, 0.1 to 20 g activating agent concentrate /I pre- or post-treatment , particularly preferably 1 to 6 g activating agent concentrate /I pre- or post-treatment .
  • Step (F) of the method according to the invention comprises the application of activation particles to the formed component from step (E).
  • activation particles are applied in step (F) and before and/or during step (B) and/or before and/or during step (C) in order to improve the nucleation process of the subsequent phosphating.
  • the additional application of crystallization nuclei increases the number of nucleation sites on the substrate, since the zinc phosphate precipitating from the phosphating solution preferentially crystallizes on the additional nuclei.
  • the number of phosphate crystals per unit area is increased, so that the crystals are increasingly hindered in their growth. This leads to a reduction in crystal size and weight per unit area, while the crystal formation rate increases and the degree of coverage increases.
  • the phosphate layer is formed more evenly and the consumption of chemicals can be reduced.
  • the crystals become mechanically more stable and the adhesion of the crystals to the substrate is improved.
  • the formation of smaller, evenly distributed phosphate crystals leads to an improvement in the adhesion of the paint film applied in the subsequent process.
  • the phosphating process can therefore be precisely adjusted and controlled.
  • the actual activation step is generally preceded by a separate cleaning step in which the surface is first freed of electrolyte, oils, fats, solid particles, oxides and other contaminants using an alkaline or acidic cleaner.
  • the pH range can be between 6 and 13.
  • the surface is then rinsed with fresh water and deionized water to prevent carryover into the subsequent activation bath.
  • the additional activation particles that are applied in step (F) of the process according to the invention are preferably selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides.
  • water-dispersible compounds are used, for example oxalates of silver or copper compounds, disodium phosphate in combination with titanium compounds, in particular with water-soluble titanium compounds, for example titanium phosphate or sodium titanyl phosphates, zinc phosphates and mixtures of zinc phosphates and metal oxides, e.g. zinc or iron oxides and mixtures thereof.
  • the additional activation particles are preferably applied in powder form.
  • the present invention therefore preferably relates to the process according to the invention, wherein the additional activation particles which are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C) are selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides.
  • the concentration of the activating agent is, for example, 0.1 to 20 g activating agent concentrate /I pre- or post-treatment , particularly preferably 1 to 6 g activating agent concentrate /I pre- or post-treatment.
  • activation particles with a concentration (powder or liquid) are thus present on the formed component after step (F) of the process according to the invention.
  • Step (G) of the process according to the invention comprises applying a phosphating to the formed component from step (F).
  • an aqueous solution containing zinc phosphate, phosphoric acid, optionally nickel and/or manganese cations, and an accelerator is preferably used.
  • the accelerator used is, for example, nitrate, for example zinc nitrate, nitrite, for example sodium nitrite, or hydrogen peroxide.
  • Step (G) of the process according to the invention is preferably carried out by immersing the formed components from step (F) in an aqueous solution containing the above-mentioned components.
  • the contact time is, for example, 100 to 200 s.
  • the process steps are preferably carried out in the order (A), (B), (C), (D), (E) and (F).
  • the process according to the invention can optionally comprise further steps, for example oiling and/or bonding, which then take place between the steps mentioned.
  • steps (C), (F) and/or (G) are preferably carried out by a spraying, dipping or coating process.
  • the application of solutions in steps (B), (C), (F), (G) of the process according to the invention, in particular the application of the additional activation particles before and/or during step (B) and/or before and/or during step (C), is preferably carried out in a coating process.
  • Coating processes are known to the person skilled in the art.
  • the ratio is preferably the rotational speed of the application roller to the belt speed 70 to 130%.
  • the temperature of the solution, in particular the aqueous solution is preferably 15 to 30 °C.
  • a wet film with a thickness of 1 to 4 ⁇ m, corresponding to 1 to 4 ml/m 2 is preferably applied. After the wet film has been applied, the coated board is preferably dried.
  • the temperature of the dryer is set so that a suitable temperature is set in relation to the belt speed, for example 60 to 130 °C.
  • the belt speed is for example 30 to 180 m/min, preferably 80 to 120 m/min, for example 100 m/min.
  • the present invention also relates to a component manufactured by the method according to the invention.
  • the components manufactured according to the invention are characterized in that they have a particularly homogeneous phosphating layer on the surface.
  • the activation causes the zinc phosphate crystals to become particularly finely crystalline, i.e. this results in lower chemical consumption, the mechanical stability is higher, which means better paint adhesion and corrosion resistance. Furthermore, the process times are shorter because small crystals crystallize out more quickly than large ones.
  • the present invention also relates to the use of a component according to the invention in the automotive sector.
  • the component according to the invention is suitable for use in the automotive sector due to its advantageous properties.
  • the concentration of the adhesion promoter is 2 to 6 (silicon coating as a conductive element) g/L.
  • a wetting agent available under the trade name H7475, is also applied.
  • activation particles available under the trade name ZL 6, are also applied.
  • the aqueous solutions are applied at a temperature of 15 to 30 °C, the wet film thickness of the applied solution is 1 to 4 ⁇ m, corresponding to 1 to 4 ml/m 2 .
  • the coated tape is dried at a temperature of 60 to 130 °C. During the process, the tape speed is 100 m/min -1 .

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Description

Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung eines umgeformten Bauteils, umfassend mindestens die Schritte (A) Bereitstellen eines Stahlflachprodukts, (B) Dressieren des Stahlflachprodukts aus Schritt (A), (C) Aufbringen einer funktionalen Beschichtung auf das Stahlflachprodukt aus Schritt (B), (D) Umformen des Stahlflachprodukts aus Schritt (C), um ein umgeformtes Bauteil zu erhalten, (E) Entfernen der funktionalen Beschichtung von dem umgeformten Bauteil aus Schritt (D), (F) Aufbringen von Aktivierungspartikeln auf das umgeformte Bauteil aus Schritt (E), und (G) Aufbringen einer Phosphatierung auf das umgeformte Bauteil aus Schritt (F), wobei vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht werden. Des Weiteren betrifft die vorliegende Erfindung ein entsprechendes Stahlflachprodukt und dessen Verwendung im Automobilsektor.The present invention relates to a method for producing a formed component, comprising at least the steps (A) providing a flat steel product, (B) skin rolling the flat steel product from step (A), (C) applying a functional coating to the flat steel product from step (B), (D) forming the flat steel product from step (C) to obtain a formed component, (E) removing the functional coating from the formed component from step (D), (F) applying activation particles to the formed component from step (E), and (G) applying a phosphating to the formed component from step (F), wherein additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C). Furthermore, the present invention relates to a corresponding flat steel product and its use in the automotive sector.

Im Stand der Technik sind Verfahren zur Verbesserung phosphatierter Oberflächen von antikorrosiv beschichteten Stahlflachprodukten oder zur Verbesserung der Haftfähigkeit solcher Oberflächen bereits bekannt.In the prior art, methods for improving phosphated surfaces of anti-corrosive coated flat steel products or for improving the adhesion of such surfaces are already known.

In der EP 2 824 213 A1 wird ein Verfahren zur Verbesserung der Haftfähigkeit auf einem antikorrosiv beschichteten Stahlblech beschrieben. Dazu wird eine wässrige, Fluorid-Ionen haltige Lösung auf die ZnO- und Al2O3-aufweisende Oxidschicht der Schutzbeschichtung auf Basis Zn-Al-Mg aufgebracht. Die Fluorid-Ionen sorgen dafür, dass die Oxidschicht modifiziert, aber dicht dekapiert wird, so dass ein anschließend aufgebrachter Kleber eine bessere Haftung zeigt.In the EP 2 824 213 A1 A process for improving the adhesion to an anti-corrosive coated steel sheet is described. For this purpose, an aqueous solution containing fluoride ions is applied to the ZnO and Al 2 O 3 -containing oxide layer of the protective coating based on Zn-Al-Mg. The fluoride ions ensure that the oxide layer is modified but densely decapitated, so that an adhesive subsequently applied shows better adhesion.

US 2015/0352825 A1 offenbart ein Verfahren, bei dem ein Stahlflachprodukt, das eine antikorrosive Beschichtung aufweist, zunächst mit einer sauren Lösung behandelt wird, damit ein anschließend aufgebrachter Kleber eine bessere Haftung zeigt. US 2015/0352825 A1 discloses a process in which a flat steel product having an anti-corrosive coating is first treated with an acidic solution so that a subsequently applied adhesive shows better adhesion.

WO 2017/125131 A1 offenbart ein Verfahren zum Herstellen eines Stahlproduktes, das eine Schutzbeschichtung auf Basis von Zink und eine auf die Schutzbeschichtung aufgetragene tribologisch aktive Schicht aufweist. WO 2017/125131 A1 discloses a method for producing a steel product having a zinc-based protective coating and a tribologically active layer applied to the protective coating.

Die aus dem Stand der Technik bekannten antikorrosiv beschichteten Stahlflachprodukte weisen oftmals das Problem auf, dass während ihrer Herstellung eine temporäre Vor- oder Nachbehandlung, d.h. eine funktionale Beschichtung wie beispielsweise eine haftvermittelnde Schicht, eine Umformhilfe, eine Passivierung oder eine Kombination daraus, aufgebracht und wieder entfernt werden muss. Dieses Entfernen erfolgt in der Regel durch einen Reinigungsschritt. Dabei kann es vorkommen, dass der Reinigungsschritt nicht vollständig verläuft, d.h., dass zumindest auf Teilflächen des Stahlflachprodukts Reste der funktionalen Beschichtung verbleiben. Bei einem anschließend durchgeführten zweistufigen Phosphatier-schritt umfassend zum einen das Aufbringen von Aktivierungspartikeln und des Weiteren das Phosphatieren, können die Aktivierungspartikel durch die vorhandenen Reste der funktionalen Schicht die eigentliche Oberfläche des Stahlflachprodukts nicht vollständig erreichen, so dass im Ergebnis eine Phosphatschicht entsteht, die in Bereichen aus unterschiedlich groß formierten Zinkphosphatkristallen besteht, welche in der makroskopischen Betrachtung ungleichmäßig erscheinen, was unerwünscht ist.The anti-corrosive coated steel flat products known from the state of the art often have the problem that during their production a temporary pre- or post-treatment, i.e. a functional coating such as an adhesion-promoting layer, a forming aid, a passivation or a combination thereof, is applied and then removed again. This removal is usually carried out by a cleaning step. It can happen that the cleaning step is not completed, i.e. that residues of the functional coating remain on at least some areas of the flat steel product. In a subsequent two-stage phosphating step, which includes the application of activation particles and phosphating, the activation particles cannot fully reach the actual surface of the flat steel product due to the residues of the functional layer, so that the result is a phosphate layer that consists in areas of zinc phosphate crystals of different sizes that appear uneven when viewed macroscopically, which is undesirable.

Aufgabe der vorliegenden Erfindung ist es daher, ein Verfahren zur Herstellung eines phosphatierten Stahlflachprodukts bereit zu stellen, welches gegenüber dem Stand der Technik verbesserte phosphatierte Oberflächen, die insbesondere eine bessere Kleberhaftung zeigen, ergibt. Insbesondere soll erfindungsgemäß ein Verfahren bereitgestellt werden, welches auch dann gute phosphatierte Oberflächen, insbesondere mit einer verbesserten Kleberhaftung, liefert, wenn zwischenzeitlich aufgebrachte funktionale Beschichtungen nicht vollständig entfernt worden sind.The object of the present invention is therefore to provide a method for producing a phosphated flat steel product which, compared to the prior art, produces improved phosphated surfaces which, in particular, exhibit better adhesive adhesion. In particular, the invention aims to provide a method which produces good phosphated surfaces, in particular with improved adhesive adhesion, even when functional coatings applied in the meantime have not been completely removed.

Diese Aufgaben werden erfindungsgemäß gelöst durch das Verfahren zur Herstellung eines umgeformten Bauteils, umfassend mindestens die folgenden Schritte:

  1. (A) Bereitstellen eines Stahlflachprodukts,
  2. (B) Dressieren des Stahlflachprodukts aus Schritt (A),
  3. (C) Aufbringen einer funktionalen Beschichtung auf das Stahlflachprodukt aus Schritt (B),
  4. (D) Umformen des Stahlflachprodukts aus Schritt (C), um ein umgeformtes Bauteil zu erhalten,
  5. (E) Entfernen der funktionalen Beschichtung von dem umgeformten Bauteil aus Schritt (D),
  6. (F) Aufbringen von Aktivierungspartikeln auf das umgeformte Bauteil aus Schritt (E), und
  7. (G) Aufbringen einer Phosphatierung auf das umgeformte Bauteil aus Schritt (F),
wobei vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht werden.These objects are achieved according to the invention by the method for producing a formed component, comprising at least the following steps:
  1. (A) Providing a flat steel product,
  2. (B) skin passing of the flat steel product from step (A),
  3. (C) applying a functional coating to the flat steel product from step (B),
  4. (D) forming the flat steel product from step (C) to obtain a formed component,
  5. (E) removing the functional coating from the formed component from step (D),
  6. (F) applying activation particles to the formed component from step (E), and
  7. (G) applying a phosphating to the formed component from step (F),
wherein additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C).

Das erfindungsgemäße Verfahren wird im Folgenden detailliert beschrieben.The method according to the invention is described in detail below.

Schritt (A):Step (A):

Schritt (A) des erfindungsgemäßen Verfahrens umfasst das Bereitstellen eines Stahlflachprodukts. Bevorzugt wird in Schritt (A) ein mit einer vor Korrosion schützenden Beschichtung versehenes Stahlflachprodukt bereitgestellt.Step (A) of the method according to the invention comprises providing a flat steel product. Preferably, in step (A), a flat steel product provided with a coating that protects against corrosion is provided.

Im Allgemeinen kann das erfindungsgemäß eingesetzte Stahlflachprodukt aus jeder dem Fachmann bekannten Stahlgüte bestehen, beispielsweise CR3 bzw. DX51. Dieser erfindungsgemäß bevorzugt eingesetzte Stahl enthält beispielsweise max. 0,08 Gew.-% C, max. 0,45 Gew.-% Mn, max. 0,030 Gew.-% P, max. 0,030 Gew.-% S, max. 0,15 Gew.-% Cr, max. 0,20 Gew.-% Cu, max. 0,06 Gew.-% Mo, max. 0,008 Gew.-% Nb, max. 0,20 Gew.-% Ni, wobei die Summe von Cu, Ni, Cr und Mo 0,50 Gew.-% nicht übersteigen darf und die Summe von Cr und Mo nicht 0,16 Gew.-% nicht übersteigen darf, Rest Fe und unvermeidbare Verunreinigungen.In general, the flat steel product used according to the invention can consist of any steel grade known to the person skilled in the art, for example CR3 or DX51. This steel preferably used according to the invention contains, for example, max. 0.08 wt.% C, max. 0.45 wt.% Mn, max. 0.030 wt.% P, max. 0.030 wt.% S, max. 0.15 wt.% Cr, max. 0.20 wt.% Cu, max. 0.06 wt.% Mo, max. 0.008 wt.% Nb, max. 0.20 wt.% Ni, where the sum of Cu, Ni, Cr and Mo must not exceed 0.50 wt.% and the sum of Cr and Mo must not exceed 0.16 wt.%, the remainder being Fe and unavoidable impurities.

Erfindungsgemäß handelt es sich bei dem erfindungsgemäßen Stahlflachprodukt um ein Warmband oder ein Kaltband. Diese können nach dem Fachmann bekannten Verfahren erhalten werden. Neben Stahlbändern können in Schritt (A) des erfindungsgemäßen Verfahrens auch so genannte Platinen eingesetzt werden, die bevorzugt erhalten werden, indem aus einem Warm- oder Kaltband durch geeignete Verfahren Stücke abgetrennt werden.According to the invention, the flat steel product according to the invention is a hot strip or a cold strip. These can be obtained by methods known to those skilled in the art. In addition to steel strips, so-called blanks can also be used in step (A) of the method according to the invention, which are preferably obtained by cutting pieces from a hot or cold strip using suitable methods.

Das erfindungsgemäße Stahlflachprodukt basiert auf einem Stahlblech, bevorzugt enthaltend eine vor Korrosion schützende Beschichtung. Die erfindungsgemäß bevorzugt vorliegende vor Korrosion schützende Beschichtung ist bevorzugt metallisch. Die Beschichtung des Stahlblechs kann in bekannter Weise erfolgen, beispielsweise im Schmelztauchverfahren (Feuerverzinkung) oder durch elektrolytische Abscheidung. Erfindungsgemäß bevorzugt erfolgt die Beschichtung im Schmelztauchverfahren. Entsprechende Verfahren sind dem Fachmann an sich bekannt.The flat steel product according to the invention is based on a steel sheet, preferably containing a coating that protects against corrosion. The coating that protects against corrosion, which is preferably present according to the invention, is preferably metallic. The steel sheet can be coated in a known manner, for example in a hot-dip process (hot-dip galvanizing) or by electrolytic deposition. According to the invention, the coating is preferably carried out in a hot-dip process. Corresponding processes are known per se to those skilled in the art.

Die Beschichtung, die auf dem erfindungsgemäßen Stahlflachprodukt bevorzugt vorliegt, basiert bevorzugt auf Zink, einer Zinklegierung, aus Aluminium oder einer Aluminiumlegierung. Erfindungsgemäß kann in Schritt (A) auch eine nicht beschichtete, insbesondere nicht verzinkte, Stahloberfläche verwendet werden.The coating that is preferably present on the flat steel product according to the invention is preferably based on zinc, a zinc alloy, aluminum or an aluminum alloy. According to the invention, a non-coated, in particular non-galvanized, steel surface can also be used in step (A).

Geeignete Beschichtungen enthalten daher beispielsweise Zink oder Zink und Magnesium, Zink und Aluminium oder Zink, welches elektrolytisch aufgebracht worden ist.Suitable coatings therefore contain, for example, zinc or zinc and magnesium, zinc and aluminium or zinc which has been applied electrolytically.

Die Beschichtung des Stahlflachprodukts, insbesondere des Stahlbands, erfolgt dabei bevorzugt, indem in einer ersten Stufe des Beschichtungsprozesses die Bandoberfläche zunächst mechanisch und/oder chemisch gereinigt wird. Anschließend wird die Bandoberfläche bevorzugt in einer sauren Beize aufgeraut, bevor das Band durch eine elektrolytische Beschichtungszelle hindurchgeleitet und dort beschichtet, insbesondere verzinkt, wird. In der Beschichtungszelle wird das Stahlband in einen schwefelsauren Zink-Elektrolyten getaucht und gleichzeitig als Kathode geschaltet. Im Falle von löslichen Elektroden werden diese ebenfalls in die Elektrolytlösung getaucht und als Anode geschaltet. Die Kationen wandern dabei von der Anode durch den Elektrolyten zu der Stahlbandoberfläche und werden dort kathodisch abgeschieden. Im Falle von unlöslichen Anoden ist dagegen das Metall, beispielsweise Zink, bereits im Elektrolyten gelöst, wobei die Anoden aus entsprechend edleren Materialien bestehen. Die auf der Bandoberfläche abgeschiedene Metallmenge hängt jeweils von der Stromdichte und der Beschichtungsdauer ab. Um bei einer Bandgeschwindigkeit von beispielsweise 100 m/min eine Metallschichtdicke von einigen Mikrometern zu erzielen, muss das Stahlband wegen der bei einer solchen Bandgeschwindigkeit relativ geringen Beschichtungsdauer und damit entsprechend geringer Abscheiderate in einer Elektrolytzelle mehrere hintereinander geschaltete Beschichtungszellen durchlaufen. Um anschließend den Elektrolyten von der Bandoberfläche zu entfernen und somit eine Elektrolytverschleppung in den nächsten Prozessschritt zu vermeiden, wird das elektrolytisch beschichtete Stahlband bevorzugt durch eine mehrstufige Spülvorrichtung hindurchgeleitet.The flat steel product, in particular the steel strip, is preferably coated by first mechanically and/or chemically cleaning the strip surface in a first stage of the coating process. The strip surface is then roughened, preferably in an acidic pickling solution, before the strip is passed through an electrolytic coating cell and coated, in particular galvanized, there. In the coating cell, the steel strip is dipped in a sulfuric acid zinc electrolyte and simultaneously switched as a cathode. In the case of soluble electrodes, these are also dipped in the electrolyte solution and switched as an anode. The cations migrate from the anode through the electrolyte to the steel strip surface and are cathodically deposited there. In the case of insoluble anodes, on the other hand, the metal, for example zinc, is already dissolved in the electrolyte, whereby the anodes consist of correspondingly more noble materials. The amount of metal deposited on the strip surface depends on the current density and the coating duration. In order to achieve a metal layer thickness of a few micrometers at a belt speed of, for example, 100 m/min, the steel strip must pass through several coating cells connected in series in an electrolytic cell because of the relatively short coating time and thus the correspondingly low deposition rate at such a belt speed. In order to then remove the electrolyte from the strip surface and thus avoid electrolyte being carried over into the next process step, the electrolytically coated steel strip is preferably passed through a multi-stage rinsing device.

Erfindungsgemäß besonders bevorzugt besteht die vorliegende Beschichtung aus Zink oder einer Zinklegierung, die weiter bevorzugt durch Schmelztauchbeschichten aufgebracht worden ist. Verfahren zur Schmelztauchbeschichtung sind dem Fachmann an sich bekannt.According to the invention, the present coating particularly preferably consists of zinc or a zinc alloy, which has more preferably been applied by hot-dip coating. Methods for hot-dip coating are known per se to those skilled in the art.

Die Beschichtung, insbesondere aus Zink oder einer Zinklegierung, liegt erfindungsgemäß bevorzugt mit einem Auflagengewicht von 1 bis 600 g/m2, d.h. 0,5 bis 300 g/m2 pro Seite, besonders bevorzugt 20 bis 300 g/m2, d.h. 10 bis 150 g/m2 pro Seite, vor.According to the invention, the coating, in particular made of zinc or a zinc alloy, is preferably present with a coating weight of 1 to 600 g/m 2 , ie 0.5 to 300 g/m 2 per side, particularly preferably 20 to 300 g/m 2 , ie 10 to 150 g/m 2 per side.

Schritt (B):Step (B):

Schritt (B) des erfindungsgemäßen Verfahrens umfasst das Dressieren des Stahlflachprodukts aus Schritt (A).Step (B) of the process according to the invention comprises the skin passing of the flat steel product from step (A).

Das Dressieren ist dem Fachmann an sich bekannt und beispielsweise beschrieben in Handbuch Umformen, Günter Spur, ISBN: 978-3-446-43004-4, Seite 155 .Dressing is known to the expert and is described, for example, in Handbook of forming, Günter Spur, ISBN: 978-3-446-43004-4, page 155 .

Bevorzugt betrifft die vorliegende Erfindung das erfindungsgemäße Verfahren, wobei das Dressieren in Schritt (B) unter Verwendung eines Dressiermittels erfolgt. In einer besonders bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens wird daher vor und/oder während Schritt (B) mindestens ein Dressiermittel auf das Stahlflachprodukt aufgebracht. Einsetzbare Dressiermittel sind dem Fachmann an sich bekannt. Bevorzugt enthält das mindestens eine Dressiermittel organische Verbindungen ausgewählt aus der Gruppe bestehend aus gesättigten Kohlenwasserstoffen, insbesondere hydriertes Naphtha, alkoxylierten Alkoholen, insbesondere 2-(2-Butoxyethoxy)ethanol, 2-(Methoxymethyloxy)propan und/oder verzweigter Poly(oxy-1,2-ethandiyl)-alpha-tridecyl-omega-Alkohol, Addukten von organischen Säuren und Aminen, beispielsweise das Addukt von 3,5,5-Trimethylhexansäure und 2-Aminoethanol, Derivaten von Fettsäuren, beispielsweise Oleoylsarkosin, Aminen, beispielsweise Dodecylpropylentriamin, Glykolen, beispielsweise Hexylenglykol, und Mischungen davon.The present invention preferably relates to the method according to the invention, wherein the skin-passing in step (B) is carried out using a skin-passing agent. In a particularly preferred embodiment of the method according to the invention, at least one skin-passing agent is therefore applied to the flat steel product before and/or during step (B). Usable skin-passing agents are known per se to the person skilled in the art. Preferably, the at least one dressing agent contains organic compounds selected from the group consisting of saturated hydrocarbons, in particular hydrogenated naphtha, alkoxylated alcohols, in particular 2-(2-butoxyethoxy)ethanol, 2-(methoxymethyloxy)propane and/or branched poly(oxy-1,2-ethanediyl)-alpha-tridecyl-omega-alcohol, adducts of organic acids and amines, for example the adduct of 3,5,5-trimethylhexanoic acid and 2-aminoethanol, derivatives of fatty acids, for example oleoylsarcosine, amines, for example dodecylpropylenetriamine, glycols, for example hexylene glycol, and mixtures thereof.

Ganz besonders bevorzugt ist das mindestens eine Dressiermittel ausgewählt aus der Gruppe bestehend aus Zusammensetzungen mit den Handelsnamen Friocut LF 280, Gardolube L 8256, QWERL 4305 und Mischungen davon.Most preferably, the at least one dressing agent is selected from the group consisting of compositions with the trade names Friocut LF 280, Gardolube L 8256, QWERL 4305 and mixtures thereof.

In einer bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens wird vor und/oder während Schritt nicht nur mindestens ein Dressiermittel aufgebracht, sondern es werden gleichzeitig oder getrennt von dem mindestens einen Dressiermittel vor und/oder während Schritt (B) zusätzliche Aktivierungspartikel aufgebracht.In a preferred embodiment of the method according to the invention, not only is at least one dressing agent applied before and/or during step, but additional activation particles are applied simultaneously or separately from the at least one dressing agent before and/or during step (B).

Die vorliegende Erfindung betrifft daher bevorzugt das erfindungsgemäße Verfahren, wobei vor und/oder während Schritt (B) mindestens ein Dressiermittel und zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht werden.The present invention therefore preferably relates to the process according to the invention, wherein at least one skin-pass agent and additional activation particles are applied to the flat steel product before and/or during step (B).

In einer erfindungsgemäß bevorzugten Ausführungsform wird vor und/oder während Schritt (B) eine Mischung enthaltend mindestens ein Dressiermittel und zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht.In a preferred embodiment according to the invention, a mixture containing at least one skin-pass agent and additional activation particles is applied to the flat steel product before and/or during step (B).

In einer weiteren erfindungsgemäß bevorzugten Ausführungsform werden vor und/oder während Schritt (B) getrennt voneinander mindestens ein Dressiermittel und zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht.In a further preferred embodiment according to the invention, at least one skin-pass agent and additional activation particles are applied separately to the flat steel product before and/or during step (B).

Das mindestens eine Dressiermittel wird im Allgemeinen in einer Menge auf das Stahlflachprodukt aufgebracht, dass der nachfolgende Dressierschritt vorteilhaft ablaufen kann. Bevorzugt wird das mindestens eine Dressiermittel in einer Menge von 1 bis 50 g/L, besonders bevorzugt 10 bis 30 g/L, aufgebracht.The at least one skin-pass agent is generally applied to the flat steel product in an amount such that the subsequent skin-pass step can proceed advantageously. Preferably, the at least one skin-pass agent is applied in an amount of 1 to 50 g/L, particularly preferably 10 to 30 g/L.

Das Aufbringen des mindestens einen Dressiermittels und ggf. der Aktivierungspartikel kann im Allgemeinen nach allen dem Fachmann bekannten Verfahren erfolgen, beispielsweise Aufspritz-, Tauch- oder Coatingverfahren.The application of the at least one dressing agent and optionally the activation particles can generally be carried out by all methods known to the person skilled in the art, for example spraying, dipping or coating methods.

Entsprechende zusätzliche Aktivierungspartikel, die vor und/oder während Schritt (B) aufgebracht werden können, werden detailliert weiter unten beschrieben.Appropriate additional activation particles that may be applied before and/or during step (B) are described in detail below.

Schritt (C):Step (C):

Schritt (C) des erfindungsgemäßen Verfahrens umfasst das Aufbringen einer funktionalen Beschichtung auf das Stahlflachprodukt aus Schritt (B).Step (C) of the process according to the invention comprises applying a functional coating to the flat steel product from step (B).

Das Stahlfachprodukt, welches nach dem Dressieren in Schritt (B) erhalten wird, enthält auf der Oberfläche mindestens Teile des ggf. aufgebrachten Dressiermittel und gegebenenfalls zusätzliche Aktivierungspartikel.The steel product obtained after the skin passing in step (B) contains on the surface at least parts of the possibly applied skin passing agent and, if applicable, additional activation particles.

In Schritt (C) des erfindungsgemäßen Verfahrens wird auf dieses Stahlflachprodukt mindestens eine funktionale Beschichtung aufgebracht. Funktionale Beschichtungen sind dem Fachmann auch unter dem Begriff "Vor- bzw. Nachbehandlungen" bekannt. Funktionale Beschichtungen, die in dem erfindungsgemäßen Verfahren auf das Stahlflachprodukt aufgebracht werden können, sind dem Fachmann an sich bekannt und beispielsweise ausgewählt aus der Gruppe bestehend aus haftvermittelnder Schicht, Umformhilfe, Passivierung oder einer Kombination daraus.In step (C) of the method according to the invention, at least one functional coating is applied to this flat steel product. Functional coatings are also known to the person skilled in the art under the term "pre- or post-treatments". Functional coatings that can be applied to the flat steel product in the method according to the invention are known to the person skilled in the art and are selected, for example, from the group consisting of adhesion-promoting layer, forming aid, passivation or a combination thereof.

Geeignete haftvermittelnde Beschichtungen (Haftvermittler) sind dem Fachmann an sich bekannt und enthalten beispielsweise Alkohole, beispielsweise Methanol, Silan-Komponenten, beispielsweise Polysiloxane, Silikat-Komponenten, Ammonium- oder Aminoverbindungen, organische Polymere und Mischungen davon.Suitable adhesion-promoting coatings (adhesion promoters) are known to the person skilled in the art and contain, for example, alcohols, for example methanol, silane components, for example Polysiloxanes, silicate components, ammonium or amino compounds, organic polymers and mixtures thereof.

Ganz besonders bevorzugt ist der mindestens eine Haftvermittler ausgewählt aus der Gruppe bestehend aus Zusammensetzungen mit den Handelsnamen GBX 4537, Bonderite 1461 und Mischungen davon.Most preferably, the at least one adhesion promoter is selected from the group consisting of compositions with the trade names GBX 4537, Bonderite 1461 and mixtures thereof.

Eine haftvermittelnde Schicht kann durch alle dem Fachmann bekannten Verfahren auf das Stahlflachprodukt aufgebracht werden, beispielsweise Aufspritz-, Tauch- oder Coatingverfahren.An adhesion-promoting layer can be applied to the flat steel product by any method known to the person skilled in the art, for example spraying, dipping or coating processes.

Eine haftvermittelnde Beschichtung wird im Allgemeinen in einer Menge aufgebracht, die ausreicht, um die haftvermittelnde Wirkung zu entfalten, beispielsweise 1 mg/m2 bis 10 mg/m2, bevorzugt 2 mg/m2 bis 6 mg/m2, jeweils Auflage des Leitelementes Silizium.An adhesion-promoting coating is generally applied in an amount sufficient to exert the adhesion-promoting effect, for example 1 mg/m 2 to 10 mg/m 2 , preferably 2 mg/m 2 to 6 mg/m 2 , in each case per layer of the silicon conductive element.

Geeignete Beschichtungen, die als Umformhilfe wirken können, sind dem Fachmann an sich bekannt und enthalten beispielsweise Säuren, beispielsweise Phosphorsäure, Basen, beispielsweise Kaliumhydroxid oder organische Amine, cyclische, organische Verbindungen, beispielsweise Benzotriazol, weitere organische Verbindungen, beispielsweise Fettsäuren, Sulfonate, beispielsweise Methansulfonat, oder Alkohole, beispielsweise Aminoethanol, anorganische Salze, beispielsweise Sulfate, insbesondere Zinksulfat oder Kaliumsulfat, oder Carbonate, beispielsweise Natriumcarbonat, bevorzugt als wässrige Lösungen.Suitable coatings that can act as a forming aid are known per se to the person skilled in the art and contain, for example, acids, for example phosphoric acid, bases, for example potassium hydroxide or organic amines, cyclic organic compounds, for example benzotriazole, other organic compounds, for example fatty acids, sulfonates, for example methanesulfonate, or alcohols, for example aminoethanol, inorganic salts, for example sulfates, in particular zinc sulfate or potassium sulfate, or carbonates, for example sodium carbonate, preferably as aqueous solutions.

Ganz besonders bevorzugt ist die mindestens eine Umformhilfe ausgewählt aus der Gruppe bestehend aus Zusammensetzungen mit den Handelsnamen Lubitreat, NIT, L-FM50000, L-FM50100, L-FM50200 und Mischungen davon.Most preferably, the at least one forming aid is selected from the group consisting of compositions with the trade names Lubitreat, NIT, L-FM50000, L-FM50100, L-FM50200 and mixtures thereof.

Eine als Umformhilfe wirkende Beschichtung kann durch alle dem Fachmann bekannte Verfahren auf das Stahlflachprodukt aufgebracht werden, beispielsweise Aufspritz-, Tauch- oder Coatingverfahren.A coating acting as a forming aid can be applied to the flat steel product by any method known to the person skilled in the art, for example spraying, dipping or coating processes.

Eine als Umformhilfe wirkende Beschichtung wird im Allgemeinen in einer Menge aufgebracht, die ausreicht, um die entsprechende Wirkung zu entfalten, beispielsweise 5 mg/m2 bis 40 mg/m2, bevorzugt 10 mg/m2 bis 25 mg/m2, jeweils Auflage des Leitelementes Schwefel.A coating acting as a forming aid is generally applied in an amount sufficient to produce the corresponding effect, for example 5 mg/m 2 to 40 mg/m 2 , preferably 10 mg/m 2 to 25 mg/m 2 , in each case based on the sulfur conductive element.

Geeignete passivierende Beschichtungen (Passivierungsmittel) sind dem Fachmann an sich bekannt und enthalten beispielsweise Chromsalze, beispielsweise Chromorthophosphat, Chromnitrat, Chromtrifluorid, organische Säuren, beispielsweise Zitronensäure, anorganische Säuren, beispielsweise Fluorwasserstoffsäure, und Mischungen davon.Suitable passivating coatings (passivating agents) are known per se to the person skilled in the art and contain, for example, chromium salts, for example chromium orthophosphate, chromium nitrate, chromium trifluoride, organic acids, for example citric acid, inorganic acids, for example hydrofluoric acid, and mixtures thereof.

Ganz besonders bevorzugt ist das mindestens eine Passivierungsmittel ausgewählt aus der Gruppe bestehend aus Zusammensetzungen mit den Handelsnamen Gardolene D 6804, Gardolene D 6811, Bonderite M-PA 6003 und Mischungen davon.Most preferably, the at least one passivating agent is selected from the group consisting of compositions with the trade names Gardolene D 6804, Gardolene D 6811, Bonderite M-PA 6003 and mixtures thereof.

Eine passivierende Beschichtung kann durch alle dem Fachmann bekannten Verfahren auf das Stahlflachprodukt aufgebracht werden, beispielsweise Aufspritz-, Tauch- oder Coatingverfahren.A passivating coating can be applied to the flat steel product by any method known to the person skilled in the art, for example spraying, dipping or coating processes.

Eine passivierende Beschichtung wird im Allgemeinen in einer Menge aufgebracht, die ausreicht, um die passivierende Wirkung zu entfalten, , beispielsweise 5 mg/m2 bis 40 mg/m2, bevorzugt 10 mg/m2 bis 25 mg/m2, jeweils Auflage des Leitelementes Chrom, bei chromhaltigen Passivierungen.A passivating coating is generally applied in an amount sufficient to exert the passivating effect, for example 5 mg/m 2 to 40 mg/m 2 , preferably 10 mg/m 2 to 25 mg/m 2 , in each case based on the conductive element chromium, in the case of chromium-containing passivations.

Wird in Schritt (C) des erfindungsgemäßen Verfahrens eine Kombination der genannten funktionalen Beschichtungen gewünscht, so werden zwei oder mehr der genannten Beschichtungen in entsprechenden Mengen aufgetragen. Dies kann nacheinander oder gleichzeitig erfolgen.If a combination of the functional coatings mentioned is desired in step (C) of the process according to the invention, two or more of the coatings mentioned are applied in appropriate amounts. This can be done sequentially or simultaneously.

Bevorzugt betrifft die vorliegende Erfindung das erfindungsgemäße Verfahren, wobei vor und/oder während Schritt (C) mindestens ein funktionales Beschichtungsmittel und zusätzliche Aktivierungspartikel aufgebracht werden.The present invention preferably relates to the process according to the invention, wherein at least one functional coating agent and additional activation particles are applied before and/or during step (C).

In einer erfindungsgemäß bevorzugten Ausführungsform wird vor und/oder während Schritt (C) eine Mischung enthaltend mindestens ein funktionales Beschichtungsmittel und zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht.In a preferred embodiment of the invention, a mixture containing at least one functional coating agent and additional activation particles is applied to the flat steel product before and/or during step (C).

In einer weiteren erfindungsgemäß bevorzugten Ausführungsform werden vor und/oder während Schritt (C) getrennt voneinander mindestens ein funktionales Beschichtungsmittel und zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht.In a further preferred embodiment according to the invention, at least one functional coating agent and additional activation particles are applied separately to the flat steel product before and/or during step (C).

Details zu den zusätzlichen Aktivierungspartikeln werden weiter unten genannt.Details about the additional activation particles are given below.

Schritt (D):Step (D):

Schritt (D) des erfindungsgemäßen Verfahrens umfasst das Umformen des Stahlflachprodukts aus Schritt (C), um ein umgeformtes Bauteil zu erhalten. In der erfindungsgemäßen Ausführungsform, dass in den Schritten (A), (B) und (C) als Stahlflachprodukt ein Warmband oder ein Kaltband eingesetzt wurde, werden zu Beginn von Schritt (D) bevorzugt zunächst aus dem Warmband oder Kaltband Platinen abgeteilt. Dies kann nach dem Fachmann bekannten Verfahren erfolgen.Step (D) of the method according to the invention comprises forming the flat steel product from step (C) in order to obtain a formed component. In the embodiment according to the invention in which a hot strip or a cold strip was used as the flat steel product in steps (A), (B) and (C), blanks are preferably first cut from the hot strip or cold strip at the beginning of step (D). This can be done using methods known to those skilled in the art.

Das Umformen des Stahlflachprodukts aus Schritt (C) kann erfindungsgemäß nach allen dem Fachmann bekannten Verfahren erfolgen, beispielsweise gemäß DIN 8580 (2010) und insbesondere DIN 8584 (2010).According to the invention, the forming of the flat steel product from step (C) can be carried out by all methods known to the person skilled in the art, for example according to DIN 8580 (2010) and in particular DIN 8584 (2010).

Die Umformung findet bevorzugt bei Raumtemperatur statt.The transformation preferably takes place at room temperature.

Schritt (E):Step (E):

Schritt (E) des erfindungsgemäßen Verfahrens umfasst das Entfernen der funktionalen Beschichtung von dem umgeformten Bauteil aus Schritt (D).Step (E) of the method according to the invention comprises removing the functional coating from the formed component from step (D).

Schritt (E) des erfindungsgemäßen Verfahrens kann im Allgemeinen durch alle dem Fachmann bekannten Verfahren erfolgen, beispielsweise beschrieben in EP 2 311 928 A2 , EP 2 851 452 A1 und EP 2 937 411 A1 .Step (E) of the process according to the invention can generally be carried out by any method known to the person skilled in the art, for example described in EP 2 311 928 A2 , EP 2 851 452 A1 and EP 2 937 411 A1 .

Bevorzugt erfolgt Schritt (E) des erfindungsgemäßen Verfahrens dadurch, dass das umgeformte Bauteil aus Schritt (D) mit mindestens einem Reinigungsmittel behandelt werden kann, um die funktionale Beschichtung zu entfernen.Preferably, step (E) of the method according to the invention is carried out in that the formed component from step (D) can be treated with at least one cleaning agent in order to remove the functional coating.

Erfindungsgemäß erfolgt das Entfernen der funktionalen Beschichtung in Schritt (E) des erfindungsgemäßen Verfahrens durch Behandeln der Oberfläche des umgeformten Bauteils mit einem Reinigungsmittel. Das Reinigungsmittel kann erfindungsgemäß sauer, neutral oder alkalisch sein. In einer bevorzugten Ausführungsform wird ein alkalisches Reinigungsmittel eingesetzt.According to the invention, the functional coating is removed in step (E) of the method according to the invention by treating the surface of the formed component with a cleaning agent. According to the invention, the cleaning agent can be acidic, neutral or alkaline. In a preferred embodiment, an alkaline cleaning agent is used.

Weiter bevorzugt wird das Reinigungsmittel als wässrige Lösung eingesetzt. Dabei liegt die reinigungsaktive Substanz, beispielsweise ein Tensid, bevorzugt in einer dem Fachmann als geeignet erscheinenden Menge vor.The cleaning agent is also preferably used as an aqueous solution. The cleaning-active substance, for example a surfactant, is preferably present in an amount that appears suitable to the person skilled in the art.

Erfindungsgemäß bevorzugt vorliegende weitere Komponenten des Reinigungsmittels sind beispielsweise ausgewählt aus der Gruppe bestehend aus Natriumhydroxid oder Kaliumhydroxid und Mischungen davon.Further components of the cleaning agent which are preferably present according to the invention are, for example, selected from the group consisting of sodium hydroxide or potassium hydroxide and mixtures thereof.

Schritt (E) des erfindungsgemäßen Verfahrens kann des Weiteren unter Aufwendung mechanischer Energie erfolgen, beispielsweise indem die zu reinigenden Oberflächen gebürstet werden oder in dem Wasser und/oder Reinigungsmittel unter hohem Druck auf die Oberfläche aufgebracht werden. Schritt (E) des erfindungsgemäßen Verfahrens wird bevorzugt bei einer Temperatur von 30 bis 70 °C durchgeführt.Step (E) of the method according to the invention can also be carried out using mechanical energy, for example by brushing the surfaces to be cleaned or by applying water and/or cleaning agents to the surface under high pressure. Step (E) of the method according to the invention is preferably carried out at a temperature of 30 to 70 °C.

Bevorzugt erfolgt die Reinigung in Schritt (E) des erfindungsgemäßen Verfahrens vollständig, da dann das beste Ergebnis bei der in Schritt (G) erfolgenden Phosphatierung erzielt wird. Es wurde aber überraschenderweise gefunden, dass, wenn vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht werden, die Reinigung in Schritt (E) des erfindungsgemäßen Verfahrens nicht unbedingt vollständig sein muss, um ein besonders vorteilhaftes Ergebnis im Phosphatierschritt zu erhalten. Erfindungsgemäß gelingt es also dadurch, dass vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht werden, ein sehr gute Phosphatierergebnis zu erhalten, obwohl die funktionale Beschichtung nicht vollständig entfernt worden sein muss. Dieser Umstand vereinfacht den Prozess sehr und trägt dazu bei, qualitativ hochwertige phosphatierte und umgeformte Bauteile zu erhalten.Preferably, the cleaning in step (E) of the method according to the invention is complete, since the best result is then achieved in the phosphating in step (G). However, it has surprisingly been found that if additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C), the cleaning in step (E) of the method according to the invention does not necessarily have to be complete in order to obtain a particularly advantageous result in the phosphating step. According to the invention, by applying additional activation particles to the flat steel product before and/or during step (B) and/or before and/or during step (C), it is possible to obtain a very good phosphating result, even though the functional coating does not have to have been completely removed. This circumstance greatly simplifies the process and helps to obtain high-quality phosphated and formed components.

Das erfindungsgemäße Verfahren umfasst daher das erfindungswesentliche Merkmal, dass vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) zusätzliche Aktivierungspartikel auf das Stahlflachprodukt aufgebracht werden.The method according to the invention therefore comprises the feature essential to the invention that additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C).

Erfindungsgemäß können Sich die zusätzlichen Aktivierungspartikel von den in Schritt (F) verwendeten Aktivierungspartikeln unterscheiden. In einer weiteren erfindungsgemäß bevorzugten Ausführungsform sind die zusätzlichen Aktivierungspartikel und die in Schritt (F) des erfindungsgemäßen Verfahrens eingesetzten Aktivierungspartikel gleich.According to the invention, the additional activation particles may differ from the activation particles used in step (F). In a further preferred embodiment of the invention In this embodiment, the additional activation particles and the activation particles used in step (F) of the process according to the invention are the same.

Bevorzugt sind die zusätzlichen Aktivierungspartikel ausgewählt aus der Gruppe bestehend aus Pulveraktivierungen, insbesondere auf Basis von Titanphosphaten, oder Flüssigaktivierungen, insbesondere auf Basis von Zinkphosphaten und Metalloxiden. Bevorzugt werden in Wasser dispergierbare Verbindungen, beispielsweise Oxalate von Silber- oder Kupferverbindungen, Dinatriumphosphat in Kombination mit Titanverbindungen, insbesondere mit wasserlöslichen Titanverbindungen, beispielsweise Titanphosphat oder Natriumtitanylphosphate, Zinkphosphate und Gemische aus Zinkphosphaten und Metalloxiden z.B. Zink- oder Eisenoxide und Mischungen davon eingesetzt. Die zusätzlichen Aktivierungspartikel werden bevorzugt in Pulverform oder als wässrige Zusammensetzung aufgebracht.The additional activation particles are preferably selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides. Preferably, water-dispersible compounds are used, for example oxalates of silver or copper compounds, disodium phosphate in combination with titanium compounds, in particular with water-soluble titanium compounds, for example titanium phosphate or sodium titanyl phosphates, zinc phosphates and mixtures of zinc phosphates and metal oxides, e.g. zinc or iron oxides and mixtures thereof. The additional activation particles are preferably applied in powder form or as an aqueous composition.

Die Ansatzkonzentration des Aktivierungsmittels (pulverförmig oder als flüssiges Konzentrat) liegt beispielsweise bei 0,1 bis 20 gAktivierungsmittelkonzentrat/IVor-bzw.Nachbehandlung, besonders bevorzugt bei 1 bis 6 gAktivierungsmittelkonzentrat/IVor-bzw. Nachbehandlung.The batch concentration of the activating agent (in powder form or as a liquid concentrate) is, for example, 0.1 to 20 g activating agent concentrate /I pre- or post-treatment , particularly preferably 1 to 6 g activating agent concentrate /I pre- or post-treatment .

Schritt (F):Step (F):

Schritt (F) des erfindungsgemäßen Verfahrens umfasst das Aufbringen von Aktivierungspartikeln auf das umgeformte Bauteil aus Schritt (E).Step (F) of the method according to the invention comprises the application of activation particles to the formed component from step (E).

Erfindungsgemäß werden Aktivierungspartikel in Schritt (F) und vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) aufgebracht, um den Keimbildungsprozess der späteren Phosphatierung zu verbessern. Durch das zusätzliche Aufbringen von Kristallisationskeimen wird die Anzahl an Keimbildungsstellen auf dem Substrat erhöht, da das aus der Phosphatierungslösung ausfallende Zinkphosphat auf den zusätzlichen Keimen bevorzugt kristallisiert. Die Anzahl der Phosphatkristalle pro Flächeneinheit wird erhöht, so dass sich die Kristalle verstärkt im Wachstum behindern. Dies führt zur Verringerung von Kristallgröße und Flächengewicht, während die Kristallbildungsgeschwindigkeit steigt und sich der Bedeckungsgrad erhöht. Die Phosphatschicht wird gleichmäßiger ausgebildet und der Chemikalienverbrauch kann gesenkt werden. Die Kristalle werden mechanisch stabiler und die Haftung der Kristalle am Substrat wird verbessert. Ebenso führt die Ausbildung der kleineren, gleichmäßig verteilten Phosphatkristalle zu einer Verbesserung der Haftung des im späteren Prozess aufgebrachten Lackfilms. Der höhere Bedeckungsgrad führt zu einer geringeren Porosität, was wiederum eine gesteigerte Korrosionsresistenz mit sich bringt. Der Phosphatierungsprozess kann somit gezielt eingestellt und gesteuert werden.According to the invention, activation particles are applied in step (F) and before and/or during step (B) and/or before and/or during step (C) in order to improve the nucleation process of the subsequent phosphating. The additional application of crystallization nuclei increases the number of nucleation sites on the substrate, since the zinc phosphate precipitating from the phosphating solution preferentially crystallizes on the additional nuclei. The number of phosphate crystals per unit area is increased, so that the crystals are increasingly hindered in their growth. This leads to a reduction in crystal size and weight per unit area, while the crystal formation rate increases and the degree of coverage increases. The phosphate layer is formed more evenly and the consumption of chemicals can be reduced. The crystals become mechanically more stable and the adhesion of the crystals to the substrate is improved. Likewise, the formation of smaller, evenly distributed phosphate crystals leads to an improvement in the adhesion of the paint film applied in the subsequent process. The higher The higher the degree of coverage, the lower the porosity, which in turn increases corrosion resistance. The phosphating process can therefore be precisely adjusted and controlled.

Erfindungsgemäß geht dem eigentlichen Aktivierungsschritt im Allgemeinen ein separater Reinigungsschritt voraus, in dem die Oberfläche zunächst mit einem alkalischen oder sauren Reiniger von Elektrolyt, Ölen, Fetten, Feststoffpartikeln, Oxiden und weiteren Verunreinigungen befreit wird. Der pH-Bereich kann bei 6 bis 13 liegen. Anschließend wird die Oberfläche mit Frischwasser und deionisiertem Wasser gespült, um eine Verschleppung in das nachfolgende Aktivierungsbad zu vermeiden.According to the invention, the actual activation step is generally preceded by a separate cleaning step in which the surface is first freed of electrolyte, oils, fats, solid particles, oxides and other contaminants using an alkaline or acidic cleaner. The pH range can be between 6 and 13. The surface is then rinsed with fresh water and deionized water to prevent carryover into the subsequent activation bath.

Bevorzugt sind die zusätzlichen Aktivierungspartikel, die in Schritt (F) des erfindungsgemäßen Verfahrens aufgebracht werden, ausgewählt aus der Gruppe bestehend aus Pulveraktivierungen, insbesondere auf Basis von Titanphosphaten, oder Flüssigaktivierungen, insbesondere auf Basis von Zinkphosphaten und Metalloxiden. Bevorzugt werden in Wasser dispergierbare Verbindungen, beispielsweise Oxalate von Silber- oder Kupferverbindungen, Dinatriumphosphat in Kombination mit Titanverbindungen, insbesondere mit wasserlöslichen Titanverbindungen, beispielsweise Titanphosphat oder Natriumtitanylphosphate, Zinkphosphate und Gemische aus Zinkphosphaten und Metalloxiden z.B. Zink- oder Eisenoxide und Mischungen davon eingesetzt. Die zusätzlichen Aktivierungspartikel werden bevorzugt in Pulverform aufgebracht.The additional activation particles that are applied in step (F) of the process according to the invention are preferably selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides. Preferably, water-dispersible compounds are used, for example oxalates of silver or copper compounds, disodium phosphate in combination with titanium compounds, in particular with water-soluble titanium compounds, for example titanium phosphate or sodium titanyl phosphates, zinc phosphates and mixtures of zinc phosphates and metal oxides, e.g. zinc or iron oxides and mixtures thereof. The additional activation particles are preferably applied in powder form.

Die vorliegende Erfindung betrifft daher bevorzugt das erfindungsgemäße Verfahren, wobei die zusätzlichen Aktivierungspartikel, die vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) auf das Stahlflachprodukt aufgebracht werden, ausgewählt sind aus der Gruppe bestehend aus Pulveraktivierungen, insbesondere auf Basis von Titanphosphaten, oder Flüssigaktivierungen, insbesondere auf Basis von Zinkphosphaten und Metalloxiden.The present invention therefore preferably relates to the process according to the invention, wherein the additional activation particles which are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C) are selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides.

Die Ansatzkonzentration des Aktivierungsmittels (pulverförmig oder als flüssiges Konzentrat) liegt beispielsweise bei 0,1 bis 20 gAktivierungsmittelkonzentrat/Ivor-bzw. Nachbehandlung, besonders bevorzugt bei 1 bis 6 gAktivierungsmittelkonzentrat/IVor-bzw. Nachbehandlung-The concentration of the activating agent (powder or liquid concentrate) is, for example, 0.1 to 20 g activating agent concentrate /I pre- or post-treatment , particularly preferably 1 to 6 g activating agent concentrate /I pre- or post-treatment.

Insgesamt liegen somit auf dem umgeformten Bauteil nach Schritt (F) des erfindungsgemäßen Verfahrens Aktivierungspartikel mit einer Ansatzkonzentration (pulverförmig oder als flüssiges Konzentrat) von 0,1 bis 20 gAktivierungsmittelkonzentrat/Ivor-bzw. Nachbehandlung, besonders bevorzugt 1 bis 6 gAktivierungsmittelkonzentrat/IVor-bzw. Nachbehandlung, vor.Overall, activation particles with a concentration (powder or liquid) are thus present on the formed component after step (F) of the process according to the invention. Concentrate) of 0.1 to 20 g activating agent concentrate /I pre- or post-treatment , particularly preferably 1 to 6 g activating agent concentrate /I pre- or post-treatment .

Schritt (G):Step (G):

Schritt (G) des erfindungsgemäßen Verfahrens umfasst das Aufbringen einer Phosphatierung auf das umgeformte Bauteil aus Schritt (F).Step (G) of the process according to the invention comprises applying a phosphating to the formed component from step (F).

Die Phosphatierung von Stahlflachprodukten ist dem Fachmann an sich bekannt und beispielsweise beschrieben in Rausch, W., Die Phosphatierung von Metallen, Eugen G. Leuze Verlag, Saulgau/Württ, 2. Auflage, 1988, ISBN: 3-87480-043-1 .The phosphating of flat steel products is known to the person skilled in the art and is described, for example, in Rausch, W., The phosphating of metals, Eugen G. Leuze Verlag, Saulgau/Württ, 2nd edition, 1988, ISBN: 3-87480-043-1 .

In Schritt (G) des erfindungsgemäßen Verfahrens wird bevorzugt eine wässrige Lösung enthaltend Zinkphosphat, Phosphorsäure, gegebenenfalls Nickel- und/oder Mangankationen, und einen Beschleuniger eingesetzt. Als Beschleuniger wird erfindungsgemäß beispielsweise Nitrat, beispielsweise als Zinknitrat, Nitrit, beispielsweise als Natriumnitrit oder Wasserstoffperoxid eingesetzt.In step (G) of the process according to the invention, an aqueous solution containing zinc phosphate, phosphoric acid, optionally nickel and/or manganese cations, and an accelerator is preferably used. According to the invention, the accelerator used is, for example, nitrate, for example zinc nitrate, nitrite, for example sodium nitrite, or hydrogen peroxide.

Schritt (G) des erfindungsgemäßen Verfahrens wir bevorzugt durchgeführt, indem die umgeformten Bauteile aus Schritt (F) in eine wässrige Lösung enthaltend die oben genannten Komponenten eingetaucht werden. Die Kontaktzeit liegt dabei beispielsweise bei 100 bis 200 s.Step (G) of the process according to the invention is preferably carried out by immersing the formed components from step (F) in an aqueous solution containing the above-mentioned components. The contact time is, for example, 100 to 200 s.

Erfindungsgemäß bevorzugt werden die Verfahrensschritte in der Reihenfolge (A), (B), (C), (D), (E) und (F) durchgeführt. Das erfindungsgemäße Verfahren kann neben den genannten Verfahrensschritten (A) bis (F) gegebenenfalls weitere Schritte aufweisen, beispielsweise Beölung und/oder Verkleben, die dann zwischen den genannten Schritten erfolgen.According to the invention, the process steps are preferably carried out in the order (A), (B), (C), (D), (E) and (F). In addition to the process steps (A) to (F) mentioned, the process according to the invention can optionally comprise further steps, for example oiling and/or bonding, which then take place between the steps mentioned.

In dem erfindungsgemäßen Verfahren erfolgen die Schritte (C), (F) und/oder (G) bevorzugt jeweils durch ein Aufspritz-, Tauch- oder Coatingverfahren.In the process according to the invention, steps (C), (F) and/or (G) are preferably carried out by a spraying, dipping or coating process.

Das Aufbringen von Lösungen in den Schritte (B), (C), (F), (G) des erfindungsgemäßen Verfahrens, insbesondere das Aufbringen der zusätzlichen Aktivierungspartikel vor und/oder während Schritt (B) und/oder vor und/oder während Schritt (C) erfolgt bevorzugt in einem Coatingverfahren. Coatingverfahren sind dem Fachmann an sich bekannt. Bevorzugt beträgt dabei das Verhältnis der Umdrehungsgeschwindigkeit der Applikationswalze zur Bandlaufgeschwindigkeit 70 bis 130%. Die Temperatur der, insbesondere wässrigen, Lösung beträgt bevorzugt 15 bis 30 °C. Es wird bevorzugt ein Nassfilm mit einer Dicke von 1 bis 4 µm, entsprechend 1 bis 4 ml/m2, aufgetragen. Nach dem Auftragen des Nassfilms wird die beschichtete Platine bevorzugt getrocknet. Dabei wird die Temperatur des Trockners so eingestellt, dass in Relation zur Bandgeschwindigkeit eine passende Temperatur eingestellt wird, beispielsweise 60 bis 130 °C. Während des Beschichtens beträgt die Bandgeschwindigkeit beispielsweise 30 bis 180 m/min, bevorzugt 80 und 120 m/min, beispielsweise 100 m/min.The application of solutions in steps (B), (C), (F), (G) of the process according to the invention, in particular the application of the additional activation particles before and/or during step (B) and/or before and/or during step (C), is preferably carried out in a coating process. Coating processes are known to the person skilled in the art. The ratio is preferably the rotational speed of the application roller to the belt speed 70 to 130%. The temperature of the solution, in particular the aqueous solution, is preferably 15 to 30 °C. A wet film with a thickness of 1 to 4 µm, corresponding to 1 to 4 ml/m 2 , is preferably applied. After the wet film has been applied, the coated board is preferably dried. The temperature of the dryer is set so that a suitable temperature is set in relation to the belt speed, for example 60 to 130 °C. During coating, the belt speed is for example 30 to 180 m/min, preferably 80 to 120 m/min, for example 100 m/min.

Die vorliegende Erfindung betrifft auch ein Bauteil, hergestellt durch das erfindungsgemäße Verfahren. Die erfindungsgemäß hergestellten Bauteile zeichnen dadurch aus, dass sie eine besonders homogene Phosphatierungsschicht an der Oberfläche aufweisen. Durch die Aktivierung werden die Zinkphosphatkristalle besonders feinkristallin, d.h. es resultiert ein geringerer Chemikalienverbrauch, die mechanische Stabilität ist höher, was eine bessere Lackhaftung und Korrosionsresistenz bedeutet. Des Weiteren sind die Prozesszeiten geringer, da kleine Kristalle schneller auskristallisiert sind als große.The present invention also relates to a component manufactured by the method according to the invention. The components manufactured according to the invention are characterized in that they have a particularly homogeneous phosphating layer on the surface. The activation causes the zinc phosphate crystals to become particularly finely crystalline, i.e. this results in lower chemical consumption, the mechanical stability is higher, which means better paint adhesion and corrosion resistance. Furthermore, the process times are shorter because small crystals crystallize out more quickly than large ones.

Die vorliegende Erfindung betrifft auch die Verwendung eines erfindungsgemäßen Bauteils im Automobilbereich.The present invention also relates to the use of a component according to the invention in the automotive sector.

Gewerbliche AnwendbarkeitCommercial applicability

Das erfindungsgemäße Bauteil ist aufgrund seiner vorteilhaften Eigenschaften für den Einsatz im Automobilbereich geeignet.The component according to the invention is suitable for use in the automotive sector due to its advantageous properties.

FigurenFigures

  • Figur 1 zeigt eine Beschichtung erhalten nach Vergleichsversuch V5. Figure 1 shows a coating obtained according to comparative test V5.
  • Figur 2 zeigt eine Beschichtung erhalten nach erfindungsgemäßem Versuch 6. Figure 2 shows a coating obtained according to inventive experiment 6.
BeispieleExamples

Es werden entsprechende Stahlplatinen, welche mit einer ZM-(Zink-Magnesium)-Beschichtung auf beiden Seiten beschichtet ist, dressiert. Anschließend wird ein Haftvermittler (HM), enthaltend Methanol, ein Polysiloxan, eine Silikat-Komponente und Ammonium- oder Aminoverbindungen, erhältlich unter dem Handelsnamen GB X4537, in wässriger Lösung auf Ober- und Unterseite in einem Bandbeschichter auf das Band aufgebracht. Die Konzentration des Haftvermittlers beträgt dabei 2 bis 6 (Siliziumauflage als Leitelement) g/L. In den Versuchen 3 bis 7 wird zusätzlich ein Netzmittel, erhältlich unter dem Handelsnamen H7475, aufgebracht. In den erfindungsgemäßen Versuchen 6 und 7 werden zusätzlich Aktivierungspartikel, erhältlich unter dem Handelsnamen ZL 6, aufgebracht.Corresponding steel plates, which are coated with a ZM (zinc-magnesium) coating on both sides, are dress-rolled. Then an adhesion promoter (HM) containing methanol, a polysiloxane, a silicate component and ammonium or amino compounds, available under the trade name GB X4537, is applied to the top and bottom of the strip in an aqueous solution in a strip coater. The concentration of the adhesion promoter is 2 to 6 (silicon coating as a conductive element) g/L. In experiments 3 to 7, a wetting agent, available under the trade name H7475, is also applied. In experiments 6 and 7 according to the invention, activation particles, available under the trade name ZL 6, are also applied.

Die wässrigen Lösungen werden bei einer Temperatur von 15 bis 30 °C aufgebracht, die Nassfilmdicke der applizierten Lösung beträgt jeweils 1 bis 4 µm, entsprechend 1 bis 4 ml/m2. Nach Auftragen der Lösung wird das beschichtete Band bei einer Temperatur von 60 bis 130 °C getrocknet. Während des Verfahrens beträgt die Bandgeschwindigkeit 100 m/min-1.The aqueous solutions are applied at a temperature of 15 to 30 °C, the wet film thickness of the applied solution is 1 to 4 µm, corresponding to 1 to 4 ml/m 2 . After application of the solution, the coated tape is dried at a temperature of 60 to 130 °C. During the process, the tape speed is 100 m/min -1 .

Anschließend werden die so behandelten Platinen nach Auftragen von Aktivierungspartikeln phosphatiert. Die phosphatierten Ober- und Unterseiten werden per REM- oder EDX-Analyse begutachtet. Die Ergebnisse sind in Tabelle 1 dargestellt. Tabelle 1: Vergleichs- und erfindungsgemäße Versuche Nr. Q [%] Inhaltsstoffe der aufgebrachten wässrigen Lösung Qualität der aufgebrachten Phosphatschicht EDX-Analyse der nicht geschlossenen Bereiche V1 110 HM nicht geschlossen Hauptbestandteil Zn, zusätzlich P und Spuren von Si, Mn und Ni V2 80 HM nicht geschlossen V5 80 HM + NM nicht geschlossen V4 100 HM + NM nicht geschlossen V5 110 HM + NM nicht geschlossen 6 110 HM + NM + AP OS: geschlossen US: nicht geschlossen 7 80 HM + NM + AP OS: geschlossen US: nicht geschlossen Q Verhältnis der Umdrehungsgeschwindigkeit der Applikationswalze zur Bandlaufgeschwindigkeit HM Haftvermittler NM Netzmittel AP zusätzliche Aktivierungspartikel OS Oberseite US Unterseite V Vergleichsversuch The boards treated in this way are then phosphated after applying activation particles. The phosphated top and bottom surfaces are examined using SEM or EDX analysis. The results are shown in Table 1. Table 1: Comparative and inventive tests No. Q[%] Ingredients of the applied aqueous solution Quality of the applied phosphate layer EDX analysis of the non-closed areas V1 110 HM not closed Main component Zn, additionally P and traces of Si, Mn and Ni V2 80 HM not closed V5 80 HM + NM not closed V4 100 HM + NM not closed V5 110 HM + NM not closed 6 110 HM + NM + AP OS: closed US: not closed 7 80 HM + NM + AP OS: closed US: not closed Q Ratio of the rotational speed of the application roller to the belt running speed HM Adhesion promoter NM Wetting agent AP additional activation particles OS Top US bottom V Comparison test

Claims (11)

  1. A method for producing a formed component, comprising at least the following steps:
    (A) Providing a flat steel product,
    (B) Skin pass the steel flat product from step (A),
    (C) Application of a functional coating to the flat steel product from step (B),
    (D) Forming the steel flat product from step (C) to produce a formed component,
    (E) Removing the functional coating of step (0) from the formed component,
    (F) Application of activation particles to the formed component from step (E), and
    (G) Application of a phosphate coating to the formed component from step (F),
    characterized in that additional activation particles are applied to the flat steel product before and/or during step (B) and/or before and/or during step (C).
  2. Process according to claim 1, characterized in that in step (A) a steel flat product with a corrosion-protective coating is provided.
  3. Process according to claim 2, characterized in that the corrosion-protective coating is formed by zinc or a zinc alloy.
  4. Process according to any one of claims 1 to 3, characterized in that at least one skin pass agent and activation particles are applied to the steel flat product before and/or during step (B).
  5. Method according to any one of claims 1 to 4, characterized in that at least one functional coating agent and activation particles are applied before and/or during step (C).
  6. Method according to any one of claims 1 to 5, characterized in that the functional coating is an adhesion-promoting layer, a forming aid, a passivation or a combination thereof.
  7. Method according to one of claims 1 to 6, characterized in that steps (C), (F) and/or (G) are each carried out by a spraying, dipping or coating process.
  8. Process according to any one of claims 1 to 7, characterized in that the activation particles applied in step (F) are selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides.
  9. Process according to one of claims 1 to 8, characterized in that the additional activation particles which are applied to the steel flat product before and/or during step (B) and/or before and/or during step (C) are selected from the group consisting of powder activations, in particular based on titanium phosphates, or liquid activations, in particular based on zinc phosphates and metal oxides.
  10. A component manufactured by the method according to any one of claims 1 to 9.
  11. Use of a component according to claim 10 in the automotive sector.
EP19778901.9A 2018-09-24 2019-09-20 Method for improving the phosphatability of metal surfaces which are provided with a temporary pre- or post-treatment Active EP3856947B1 (en)

Applications Claiming Priority (2)

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DE102018216216.6A DE102018216216A1 (en) 2018-09-24 2018-09-24 Process for improving the phosphatability of metallic surfaces, which are provided with a temporary pretreatment or aftertreatment
PCT/EP2019/075340 WO2020064548A1 (en) 2018-09-24 2019-09-20 Method for improving the phosphatability of metal surfaces which are provided with a temporary pre- or post-treatment

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DE4012795A1 (en) * 1990-04-21 1991-10-24 Metallgesellschaft Ag ACTIVATING AGENT FOR PHOSPHATING
JP3857866B2 (en) * 2000-02-29 2006-12-13 日本ペイント株式会社 Non-chromate metal surface treatment agent, surface treatment method and treated painted steel
DE10110833B4 (en) * 2001-03-06 2005-03-24 Chemetall Gmbh Process for applying a phosphate coating and use of the thus phosphated metal parts
EP1350865A3 (en) * 2002-04-05 2004-12-29 ThyssenKrupp Stahl AG Tinned and phosphatised sheet and method for producing such a sheet
DE10256639A1 (en) 2002-12-03 2004-06-24 Thyssenkrupp Stahl Ag Lubricant-coated metal sheet with improved forming properties
US7947333B2 (en) * 2006-03-31 2011-05-24 Chemetall Gmbh Method for coating of metallic coil or sheets for producing hollow articles
DE102008004728A1 (en) * 2008-01-16 2009-07-23 Henkel Ag & Co. Kgaa Phosphated steel sheet and method for producing such a sheet
WO2013160568A1 (en) 2012-04-25 2013-10-31 Arcelormittal Investigacion Y Desarrollo, S.L. Method for producing a metal sheet having zn-al-mg coatings, comprising the application of an acid solution, and corresponding metal sheet
EP2824213A1 (en) 2013-07-12 2015-01-14 Voestalpine Stahl GmbH Method for improving adherence to a steel sheet with a protective coating
PL2851452T3 (en) 2013-09-19 2019-10-31 Fuchs Petrolub Se Inorganic functional coating on hot-dip galvanised steel
DE102014105226A1 (en) * 2014-04-11 2015-10-15 Thyssenkrupp Ag Method for activating metal surfaces to be phosphated, preferably galvanized sheet steel
EP2937411A1 (en) 2014-04-25 2015-10-28 Voestalpine Stahl GmbH Metal sheet and method for improving the formability of metal sheet
JP6629979B2 (en) * 2016-01-19 2020-01-15 ティッセンクルップ スチール ヨーロッパ アクチェンゲゼルシャフトThyssenKrupp Steel Europe AG Method for producing a steel product having a Zn coating and a tribologically active layer deposited on the coating, and a steel product produced according to the method

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