EP1776196A2 - Verfahren zum schützen einer metallischen oberfläche mit einer korrosions-inhibierenden beschichtung - Google Patents
Verfahren zum schützen einer metallischen oberfläche mit einer korrosions-inhibierenden beschichtungInfo
- Publication number
- EP1776196A2 EP1776196A2 EP05769621A EP05769621A EP1776196A2 EP 1776196 A2 EP1776196 A2 EP 1776196A2 EP 05769621 A EP05769621 A EP 05769621A EP 05769621 A EP05769621 A EP 05769621A EP 1776196 A2 EP1776196 A2 EP 1776196A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- anions
- coating
- poly
- depot substance
- potential
- 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.)
- Ceased
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/08—Anti-corrosive paints
- C09D5/082—Anti-corrosive paints characterised by the anti-corrosive pigment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/24—Electrically-conducting paints
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/173—Macromolecular compounds
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
- H01B1/12—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances organic substances
- H01B1/124—Intrinsically conductive polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/30—Monomer units or repeat units incorporating structural elements in the main chain
- C08G2261/31—Monomer units or repeat units incorporating structural elements in the main chain incorporating aromatic structural elements in the main chain
- C08G2261/312—Non-condensed aromatic systems, e.g. benzene
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D13/00—Electrophoretic coating characterised by the process
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/25—Web or sheet containing structurally defined element or component and including a second component containing structurally defined particles
- Y10T428/254—Polymeric or resinous material
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2913—Rod, strand, filament or fiber
- Y10T428/2927—Rod, strand, filament or fiber including structurally defined particulate matter
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31533—Of polythioether
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31605—Next to free metal
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31678—Of metal
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31678—Of metal
- Y10T428/31692—Next to addition polymer from unsaturated monomers
- Y10T428/31699—Ester, halide or nitrile of addition polymer
Definitions
- the invention relates to a method for protecting a metallic surface with a coating of a corrosion-inhibiting composition which is applied to a metallic surface, which is then optionally dried ge and optionally also cured.
- This composition contains at least one depot substance, e.g. an electrically conductive polymer which, in the event of a change in potential, releases anions which inhibit the anodic or / and cathodic partial reaction of corrosion or / and adhesion-promoting anions, so that at least partially prematurely or early, before a strong delamination occurs, or Progression of delamination is counteracted.
- a coating can often meet the criteria of an intelligent coating, as it reacts only when needed.
- EP-A1-1 382 721 protects processes for the corrosion inhibition of metallic surfaces, in which depot substances based on polyanilines are used together with derivatives of mono- and dithiol-organic acids which are incorporated as anions. Although a galvanic coupling between defect and coating is postulated as the release mechanism, only a reduction of oxygen and an associated increase in pH are described which lead to the deprotonation and release of the anions. A release of anions By lowering the potential in the polymer is neither mentioned nor suggested. The inhibiting anion is always an anion of an acid.
- the inhibiting anion unlike the present application, is released only via a protonation reaction (eg, an emeraldine salt breaks down into an emeraldine base and into a Brönsted acid containing the anion) rather than a redox reaction.
- a protonation reaction eg, an emeraldine salt breaks down into an emeraldine base and into a Brönsted acid containing the anion
- US-B1-6,328,874 describes methods of protecting an aluminum surface under electrochemical polymerization and deposition of conductive polymer at very high anodic potentials, e.g. at 15 to 60 V. However, no anion can be liberated from the film produced by reduction because too large multi-functional polymeric organic anions are used.
- DE-A1-43 34 628 C2 discloses a process for the passivation of structural steel with conductive polymer, in particular polyaniline, which is applied as a dispersion to the metallic substrate.
- conductive polymer in particular polyaniline
- the coated substrate is immersed in oxygen-containing water and passivated. Coating and passivation are carried out in separate steps. Anions are not addressed in connexion with the conductive polymer.
- the object is achieved by a method for protecting a metallic surface with a coating of a corrosion-inhibiting composition, which is optionally dried after application and optionally also gehär ⁇ tet, which is characterized in that a coating is applied to the metallic surface optionally as component (s) at least partially in a matrix
- a) contains at least one depot substance, such as at least one conductive polymer, which contains at least one type of incorporated anions as doping ions via an oxidation reaction and the second liberates at least a portion of these anions in the event of a potential decrease, at least one species being used the anions is suitable for inhibiting an anodic or / and a cathodic partial reaction of the corrosion and if appropriate also acting as an adhesion agent, the anions each having a free-wheel radius which determines their migration through the depot substance (s) and optionally through at least one further component, for example in a matrix of the coating, is not or not substantially impaired, with at least one type of anion being / being selected in such a way that these anions are present in water, in at least one other polar solvent and / or in at least one non-polar solvent enthal ⁇ border mixture are mobile, wherein the release of vo n anions from at least one depot sub- and / or only subordinate via a deprotonation reaction, but predominantly
- At least one depot substance which at least partially serves as matrix for at least one depot substance, such as e.g. at least one organic polymer / copolymer, wherein the at least one depot substance is at least partially oxidized or at least partly doped with anions in the undisturbed regions of the coating and at least one depot substance is at least partially reduced in the disturbed regions of the coating or is at least partially released from the doping anions,
- the coating of the selection of the components contained and their contents is / is adjusted so that a substantial proportion of korrosions ⁇ protecting anions and optionally also of adhesion promoting anions from at least one depot substance is released at a potential reduction between the redox potential of at least one depot substance in the undisturbed state to the corrosion potential of the metallic surface on a defect such as on a scratch or contamination at the metal / coating interface, so that at least in part prematurely or early, before a strong delamination occurs at the metal / coating interface, the onset and / or progression of the delamination is counteracted.
- the object is also achieved by a method for protecting a metalli ⁇ 's surface with a coating of a corrosion-inhibiting Zusam ⁇ composition, which optionally dried after application and possibly also cured, which is characterized in that a coating on the metallic surface is applied, which as component (s) optionally at least partially in a matrix
- At least one depot substance e.g. contains at least one conductive polymer which contains 1. at least one type of incorporated anions as doping ions via an oxidation reaction and the second liberates at least a portion of these anions when a potential drop (reduction), at least one kind of anions is suitable, anodic and / or to inhibit a cathodic partial reaction of the corrosion and, if appropriate, also to act as an adhesion-promoting agent, the anions each having a free-wheel radius which permits their migration through the depot substance (s) and optionally through at least one further component in a Mat ⁇ rix of the coating is not or not substantially impaired, wherein at least one kind of anions is selected thereafter that is, these anions in water, in at least one other polar solvent or / and in at least one non-polar solvent
- At least one further component or / and at least one matrix substance which at least partially serves as a matrix for at least one depot substance such as at least one organic polymer / copolymer, wherein the at least one depot substance in the undisturbed areas of the coating is at least partially oxidized or at least partially doped with anions and wherein at least one depot substance in is at least partially reduced or is at least partially released from the doping anions,
- the coating of the selection of the components contained and their contents is / is adjusted so that a substantial proportion of corrosion-protecting anions and possibly also of adhesion-promoting anions from at least one depot substance is already released at a lower potential reduction than at the potential reduction from the redox potential of this depot substance in the undisturbed state to the corrosion potential of the metallic surface on a defect such as on a scratch or on a contamination at the metal / coating interface, in particular at a lower potential drop on a front leading to delamination, so that at least partially prematurely or early, before a weak or strong delamination occurs at the metal / coating interface, the occurrence or progression of delamination is counteracted.
- adhesion-promoting anions occur, they must not or not all also be corrosion-protecting, so that in some embodiments, in addition to at least one type of corrosion-protecting anions, at least one type of adhesion-promoting anions also occurs.
- doping in the context of this application relates to the oxidative loading of the depot substance with anions.
- defect in the sense of this application is chosen further than usual with other authors, since it not only includes mechanical damage such as scratches, but also chemical contaminants such as not cleaned salt residues on the metal / coating interface or in its vicinity.
- delamination within the meaning of this application also relates to the marginal areas of a delineated area that are not yet completely delineated, but rather just want to begin their delamination, ie also the area around the defect that is usually wide. "Disturbed area", outside: weak delamination).
- defect area means the area around the defect in which, if appropriate, both the defect, the damaged area, and expiring fronts of the potential change are included, so changes in the chemical system have occurred. Outside the disturbed area lie undisturbed areas. Weak delamination occurs near the advanced cathodic front, where polymer adhesion has not yet been destroyed, but often oxygen reduction occurs at the interface, causing severe delamination
- the "metal / coating interface” encompasses all boundary surfaces which lie in the region of the metallic surface and the coating containing the depot substance according to the invention, Thus, for example, pretreatment layers and / or oxide-containing layers, which are partially unaided or not controlled, and their interfaces to adjacent coatings or metallic material.
- molybdate anions have been released due to a potential drop in the conductive polymer located in the disturbed region and have migrated directly to the defect. Other trails can be excluded in this experiment.
- a molybdate-containing passivation layer was then formed on the metallic surface at the damaged point and determined by XPS measurements (X-ray spectroscopy).
- FIG. 2 of DE 102004037542 results in a measurement of a strong passivation effect of a damaged one Area reproduces.
- FIG. 2 shows in comparison the general occurring effects.
- This potential reduction is preferably at least 40 mV or at least 80 mV lower than the potential reduction from the redox potential of this depot substance in the undisturbed state to the corrosion potential of the metallic surface at a defect, more preferably at least 120 mV or at least 160 mV lower, very particularly preferably at least 200 mV or at least 240 mV lower, in particular by at least 280 mV or by at least 320 mV lower.
- At least one educt for producing the depot substance (s) is preferably selected according to the following: 1. in water, in at least one other polar solvent and / or in one at least one non-polar solvent-containing mixture can be polymerized or could or was, particularly preferably in water or in a water and at least one second solvent-containing mixture.
- the proportion of released corrosion-protecting anions is essential if so many anti-corrosive anions are released that at least partially a corrosion-protective effect occurs.
- An at least low content of water or / and at least one other polar solvent in the educt mixture or in the product mixture or in the solvent mixture of the educt mixture or the product mixture is particularly preferred, including the anions in solution to bring or facilitate their migration in principle.
- the solvent mixture containing water or / and at least one other polar solvent may also be an emulsion or / and a suspension.
- the oxidation potential of the water-contacting product should preferably not be higher than the decomposition potential of water or / and at least one other polar solvent.
- the curing of the coating can be carried out by methods known per se, in particular with thermal and / or radical crosslinking. Alternatively or additionally, it is also possible to choose a film, in particular if the content of at least one filmable organic polymer and, if appropriate, also of at least one film-forming assistant is present.
- the matrix may, but not necessarily, be more pronounced or / and delineated by at least one depot substance.
- At least one further component which may be embedded in the matrix and / or belong to the matrix, for example in each case at least one hardener, a type of inorganic particles, a silane / siloxane, a polysiloxane, may also be present Corrosion inhibitor, a crosslinking agent and / or an additive.
- at least one further component may be mixed at least with the at least one depot substance.
- the coating according to the invention may, at least in part, form a matrix, for example in the case of an intercalated structure.
- the coating according to the invention can consist largely, essentially or completely of at least one depot substance and optionally at least one further component; This coating is often a more or less uniform or substantially uniform coating that is substantially or wholly without a matrix.
- a gradient coating may also be present or a virtually separate first coating on the metallic surface, predominantly, substantially or in the consists essentially of at least one depot substance and a second coating, which consists predominantly, substantially or substantially of at least one further component, wherein the second coating may optionally also contain at least one depot substance.
- a coating according to the invention which consists only or essentially only of at least one depot exists. If appropriate, low contents, in particular of at least one of the substances mentioned in this application or / and at least one reaction product, can occur here.
- At least one further coating in particular at least one organic coating such as, for example, a primer or a multilayer lacquer system or an adhesive layer, can also be applied to this coating according to the invention.
- at least one pretreatment layer is applied to the cleaned or clean metallic surface before application of the depot substance-containing composition according to the invention before a depot substance-containing coating is applied, for example to prevent flashrust, for example on steel surfaces, to increase the corrosion protection and / or to improve adhesion to the subsequent coating.
- the types of pretreatment layers or of the subsequent coatings which are advantageously to be applied to the coating according to the invention, their production processes and their properties are known in principle.
- the composition according to the invention is preferably a solution, an emulsion or / and a suspension. It preferably contains at least at the time of the polymerization at least a small amount of water and / or at least one other polar solvent, if appropriate also in a solvent mixture, with at least one further nonpolar solvent.
- the composition also contains at least one organic solvent.
- the composition optionally contains at least 2 or at least 5% by weight of water or / and at least 2 or at least 5% by weight of a polar solvent other than water, possibly in a solvent mixture, in a suspension or / and in a Emulsion.
- At least one depot substance as component of the composition or the coating is already extensively or completely polymerized after application of the coating.
- at least one depot substance is present in water or in a mixture containing water, this water optionally also being mixed in a solvent mixture, in a suspension which can be present in an emulsion, largely, almost completely or completely polymerized.
- the production processes of depot substances are known in principle.
- at least one depot substance based on at least one conductive polymer which can incorporate oxidative anions is added to the composition.
- no conductive polymer or only a small portion of the conductive polymer used is prepared or used, into or into which, for example frequently based on polyaniline, anions via a protonation reaction (eg emeraldine -Base and Brönstedt acid containing the anion, form emeraldine salt), but only or predominantly conductive polymer into which anions are incorporated via an oxidation reaction.
- a protonation reaction eg emeraldine -Base and Brönstedt acid containing the anion, form emeraldine salt
- the at least one matrix substance can-but does not have to-form, at least in one part of the coating, a matrix which optionally contains at least one further component.
- the at least one matrix substance may in particular be at least one organic or / and inorganic substance such as a film-forming component, eg organic binders and / or inorganic binders such as based on synthetic resins, natural resins, SiO 2 , water glass variants , inorganic silicates, organic silicates such as alkyl silicates, silanes, siloxanes, polysiloxanes, silylated polymers, plasticizers such as based on phthalates, reactive diluents such as based on styrene or / and caprolactam, crosslinkable - so-called "drying" - oils, Polysaccharides or / and mixtures thereof
- at least one surfactant may also be added to the mixture.
- the at least one starting material can be selected, in particular, from unsubstituted or / and substituted compounds based on imidazole, naphthalene, phenanthrene, pyrrole, thiophene or / and thiophenol. Among the unsubstituted E- products in particular pyrrole is preferred. If appropriate, at least one starting material is also prepared separately in advance and / or added to the composition in rare cases. Usually, however, at least one depot substance is added to the composition.
- At least one compound is particularly preferably selected from benzimidazoles, 2-alkylthiophenols, 2-alkoxythiophenols, 2,5-dialkylthiophenols, 2,5-dialkoxythiophenols, 1-alkylpyrroles, in particular having 1 to 16 C atoms, Alkoxypyrroles, in particular having 1 to 16 C atoms, 3-alkylpyrroles, in particular having 1 to 16 C atoms, 3-alkoxypyrroles, in particular having 1 to 16 C atoms, 3,4-dialkylpyrroles, in particular having 1 to 16 C atoms, 3, 4- Dialkoxypyrrolen in particular with 1 to 16 C-atoms, 1, 3,4-Trialkylpyrrolen in particular with 1 to 16 C-atoms, 1, 3,4-Trialkoxypyrrolen in particular with 1 to 16 C-atoms, 1-Arylpyrrolen, 3-arylpyrroles, 1-aryl-3-alkyl
- At least one compound can be selected based on pyrrole-1-ylalkylphosphonic acid, in particular having 1 to 16 C atoms, pyrrol-1-ylalkyl phosphoric acid, in particular having 1 to 16 C atoms, pyrrol-3-ylalkylphosphonic acid, in particular 1 to 16 carbon atoms, pyrrol-3-ylalkylphosphorklare in particular with 1 to 16 C-atoms, 5-alkyl-3,4-ethylendioxythiophene in particular with 1 to 12 C-atoms, 5- ( ⁇ -phosphono) alkyl-3,4 ethylenedioxythiophene and its derivatives, in particular having 1 to 12 carbon atoms, which are prepared, used as the basis for the preparation of the depot substance or added to the composition.
- the number of C atoms can each independently be 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15 or / and 16.
- substituted starting materials very particular preference is given to choosing at least one compound from 2-methylthiophenol, 2-methoxythiophenol, 2,5-dimethylthiophenol, 2,5-dimethoxythiophenol, 1-methylpyrrole, 1-ethylpyrrole, pyrrol-1-ylalkylphosphonic acid in particular with 10 or / and 12 C atoms, pyrrol-1-ylalkyl phosphate, in particular with 12 C atoms, 1-methoxypyrrole, 1-ethoxypyrrole, pyrrol-3-ylalkylphosphonic acid, in particular with 6, 8 or / and 11 C atoms , 3-methoxy-pyrrole, 3-ethoxypyrrole, 3,4-dimethylpyrrole, 3,4-dimethoxypyrrole, 1, 3,4-trimethylpyrrole, 1, 3,4-trimethoxypyrrole, 1-phenylpyrrole, 3-phenylpyrrole, 1-phenyl 3-methylpyrrole, 1-phenyl 3-methyl
- At least one compound selected from ethylthiophene, ethylenedioxythiophene, methylthiophene, 3-ethylpyrrole, 3-methylpyrrole, N-ethylpyrrole, N-methylpyrrole, 3-phenylpyrrole and their derivatives is prepared, used as the basis for the preparation of the depot substance or added to the composition.
- the conductive polymers are electrically neutral in the reduced state. During the oxidation of the conductive polymers, cations form, which can absorb correspondingly anions.
- the oxidized state can be chemically adjusted with at least one oxidizing agent, electrochemically and / or photochemically. Preferably, in this case only or largely only works chemically. Preferably, no electropolymerization is carried out, but chemically polymerized.
- the conductive polymers have a salt-like structure, so that salts can be spoken of in the case of anion-loaded conductive polymers.
- At least one depot substance is preferably at least one conductive polymer, in particular at least one conductive polymer based on imidazole, naphthalene, phenanthrene, pyrrole, thiophene or thiophenol, especially based on pyrrole or / and thiophene.
- the preferred conductive polymers include, for example, those based on polypyrrole (PPy), polythiophene (PTH), poly (para-phenylene) (PPP) or / and poly (para-phenylenevinylene) (PPV).
- the depot substance is either prepared separately or in a mixture in advance and then added to the composition and / or in rare cases added as starting material to the composition and / or reacted in the Zusam ⁇ composition and / or in the coating to depot substance.
- poly (3-alkylbithiophene) especially having 1 to 16 C atoms poly (3,3'-dialkylbithiophene), poly (3,3'-dialkoxybithiophene), poly (alkylterthiophene), poly (alkoxyterthiophene) , Poly (3,4-ethylenedioxythiophene) (PEDOT) and poly (benzo [b] thiophene (PBTH).
- composition selected from poly (1-methylpyrrole) (PI MPy), poly (1-methoxypyrrole) (PI MOPy), poly (3-methylpyrrole) (P3Mpy), poly (3-methoxy-pyrrole) (P3MOPy), poly (I -phenylpyrrole) (PI PhPy), poly (3-phenylpyrrole) (P3PhPy), Poly (3-methylthiophene), poly (3-hexylthiophene) (P3HT), poly (3-methoxythiophene), poly (3-hexoxythiophene), poly (3-phenylthiophene), poly (3-methylbithiophene), poly (3-hexylbithiophene) ), Poly (3,3'-dimethylbithiophene), poly (3,3'-dihexylbithiophene), poly (3,3'-dimethoxybithiophene),
- compounds are in each case prepared or used independently of one another with alkyl chains having 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15 or / and 16 C atoms
- the polymers may also be poly (1,3-dialkylpyrrole), poly (3,4-dialkylpyrrole), poly (3,4-dialkylthiophene), poly (1,3,4-trialkylpyrrole), poly (3,4 Dialkoxythiophene), poly (1,3,4-trialkoxypyrrole), poly (2-arylthiophene), in each case independently of one another, in particular with 1 to 16 C atoms, or corresponding starting materials are selected.
- the aryl compounds in particular 1-phenyl, 3-phenyl, 1-biphenyl, 3-biphenyl, 1- (4-azobenzene) - or / and 3- (4-azobenzene) compounds can be selected.
- the conductive polymers which are suitable for this purpose are generally known in principle, they are in some cases not yet described as being suitable for at least one variant of the corrosion protection. However, where the corrosion protection for this polymer is described be ⁇ , the corrosion protection does not work on lower metallic surfaces without existing passivation layer.
- at least one depot substance can also at least partially form a matrix in the composition, in particular near the metal / coating interface. Most conductive polymers are not commercially available.
- a conductive polymer modified by substituents or / and by another base molecule (monomer / oligomer) and / or a conductive copolymer comprising at least two different base molecules (monomers / oligomers) with somewhat different redox potentials, in order to reduce the redox properties of the depot substance to vary significantly from compound to compound.
- correspondingly different depot substances can be mixed together. In this way, at least one compound can be selected which has the correct level of redox potential for the chemical system including the metallic surface.
- the redox potential of the depot substance is particularly suitable when it is at least 75 mV, at least 100 mV or at least 150 mV, preferably at least 200 mV or at least 250 mV, very particularly preferably at least 300 mV or at least 350 mV above the corrosion potential of metallic surface lies.
- a depot substance may in principle have been polymerized chemically, electrochemically and / or photochemically.
- the at least one depot substance or the composition containing it is preferably applied electrochemically and / or mechanically, in particular to the metallic surfaces.
- the comparatively less noble metallic surfaces must first be passivated in order to prevent the high degree of dissolution of the metallic substances.
- corrosion-inhibiting anions of the solution from which at least one starting material is polymerized must always be added or added in order to always first form a passivation layer.
- the conductive polymer formed in this way thus automatically contains corrosion-inhibiting anions, but the publications which describe corrosion-inhibiting anions never indicate a release of these ions due to a lowering of the potential.
- at least one depo substance and at least one anion are selected which enable a substantial or complete release of the anions from the depot substance, whereby the cation transport rates of the cations, in particular from the electrolyte and / or from the defect, are markedly lowered which in turn can reduce the formation of harmful radicals in the area of the metal / coating interface.
- At least one oxidant is usually required in addition to at least one starting material and at least one anion which can be incorporated into the depot substance, unless an agent such as, for example, at least one added anion acts as an oxidizing agent.
- the oxidizing agent for example, at least one compound based on acids, the salts of which may exist in several valence states, e.g. Iron salts based on peroxides or / and peracids, such as e.g. Peroxodisulfate be used.
- the anions which can be incorporated oxidatively into the depot substance (s) can in particular be selected from those based on alkanoic acids, arenic acids, boron-containing acids, fluorine-containing acids, heteropolyacids, isopolyacids, iodine-containing acids, silicic acids, Lewis acids, mineral acids, Molybdenum-containing acids, peracids, phosphorus-containing acids, vanadium-containing acids, tungsten-containing acids, their salts and mixtures thereof.
- the at least one type of corrosion-protecting mobile anions is preferably at least one based on benzoate, carboxylate such as lactate, dithiol, fumarate, complex fluoride, lanthanate, metaborate, molybdate, a nitro compound such as based on nitrosalicylate Octanoate, phosphoric oxyanions such as phosphate and / or phosphonate, phthalate, salicylate, silicate, sulfoxylate such as formaldehyde sulfoxylate, thiol, titanate, vanadate, tungstate or / and zirconate, more preferably mini- at least one anion based on titanium complex fluoride or / and zirconium complex fluoride.
- carboxylate such as lactate, dithiol, fumarate, complex fluoride, lanthanate, metaborate, molybdate
- a nitro compound such as based on nitrosalicylate
- phosphoric oxyanions
- the at least one type of adhesion-promoting anions is preferably at least one phosphorus-based oxyanion, e.g. Phosphonate, silane, siloxane, polysiloxane or / and surfactant.
- the at least one type of corrosion-inhibiting and / or adhesion-promoting anions is preferably a mixture of at least two types of anions, more preferably one based on at least one of the above-mentioned anti-corrosive mobile anions of at least one kind the above-mentioned adhesion-promoting Anio ⁇ NEN, in particular selected from those based on carboxylate, complex fluoride, molybdate, nitro compound, phosphonate, polysiloxane, silane, siloxane or / and surfactant, most preferably one based on at least one of the above-mentioned anti-corrosive mobile anions with at least one kind of the above-mentioned adhesion-promoting anions.
- anion species selected from anionic types on the one hand based on carboxylate, complex fluoride, molybdate and nitro compound and on the other hand based on phosphorus-containing oxyanions, polysiloxane, silane, siloxane or / and surfactants.
- At least one kind of releasable anions is preferably one which is mobile in water, in at least one other polar solvent or / and in a solvent mixture with at least one polar solvent. It is particularly preferred that the at least one type of releasable An ⁇ ion in water, in at least one other polar solvent or / and in a solvent mixture having at least one polar solvent is at least in small amount soluble, so that it is advantageous if water, at least another polar solvent or / and an at least one polar solvent-containing Lö ⁇ seffengemisch for dissolving anions are present.
- the anions need not be anions of an acid, but may also be, for example, anions of a salt.
- Electrolyte are ions in water or in at least one polar solvent, which is optionally part of a solvent mixture, wherein the ions and water and / or at least one other polar solvent preferably - and be it in small quantities - are present.
- the corrosion-inhibiting or adhesion-promoting anions are preferably released at a potential drop of less than 700 mV, in particular to a significant extent, more preferably less than 650 mV, most preferably less than 600 mV, especially less than 550 mV, 500 mV or 450 mV.
- the corrosion-inhibiting or adhesion-promoting anions are preferably released even at a potential drop of less than 400 mV, in particular to a significant extent, more preferably less than 350 mV, most preferably less than 300 mV, especially less than 250 mV, 200 mV, 150 mV or 100 mV.
- the composition also preferably comprises at least one adhesion promoter, wherein at least one adhesion promoter optionally forms adhesion bridges between coating and metallic surface at points of delamination which stop the delamination and / or reverse.
- adhesion promoter optionally forms adhesion bridges between coating and metallic surface at points of delamination which stop the delamination and / or reverse.
- the adhesion promoter is preferably at least one substance based on compounds having at least one adhesion-promoting anchor group, in particular based on phosphonate, silane, siloxane, polysiloxane or / and surfactant.
- the adhesion promoter is particularly preferably at least one substance based on alkyl phosphonate and / or aryl phosphonate.
- the composition preferably also contains at least one radical scavenger such as e.g. at least one amine which can take up free radicals which are formed during the oxygen reduction, whereby the delamination can be stopped or slowed down.
- at least one radical scavenger such as e.g. at least one amine which can take up free radicals which are formed during the oxygen reduction, whereby the delamination can be stopped or slowed down.
- the coating according to the invention may, in the case of an organic polymeric coating, be water-dilutable and optionally also have at least one water-soluble constituent, e.g. in order to control the moisture ventilation and thereby create conditions for the ion migration in pore channels.
- polymers containing anionic groups are preferably added. Since the charge and the effective ion size often have an influence on the rate of migration, it is often preferred to use anions of lower valency.
- the metallic surface is preferably first thoroughly cleaned, in particular in such a way that the metallic surface is cleaned to be pure metal, so that all or substantially all of them are not firmly bonded. bordering and non-surface foreign matter are removed.
- complete or almost complete wetting with the treatment liquid or composition according to the invention can also be achieved.
- the composition of the cleaner on the type of pollution is particularly adapted to be particularly suitable for the application of an intermediate layer or depot substance-containing coating.
- the cleaning may also be assisted by mechanical aids such as brushes during cleaning, electrolytically and / or by ultrasound.
- At least one polymer / copolymer is preferably directly on the metallic surface and directly under the Be ⁇ least one depot substance-containing coating a subbing intermediate layer with OH "groups listed introduced, in particular by applying at least one surfactant, at least one phosphorus-containing oxyanion such as phosphonate and / or at least one silane / siloxane / polysiloxane.
- At least one further coating in particular at least one organic coating or / and at least one adhesive-containing layer, if appropriate at least one curable organic coating, such as e.g. a primer or at least one Lack ⁇ layer applied.
- a possibly improved passivation layer may possibly be formed on account of the positive "nobler" potential of the depot substance (s) compared to the negative "less noble” potential of the metallic surface and is preferably an oxide layer of the metals of the metallic surface, as described, for example, by Wessling for Polyaniline has been described.
- the oxide layer formed by the galvanic contact on the metalli ⁇ surface may interfere with the adhesion of the conductive polymer.
- an oxidic passivation in the case of samples according to the invention can not be ruled out when the coating according to the invention is applied.
- An enhancement of the passivation layer is generally considered to be relatively unefficient.
- the corrosion potential at the defect on the metallic surface is increased to a slightly higher potential, e.g. often in the range of -200 to 0 mV for steel, while it may be lower for a large defect on the metallic surface, e.g. in the case of steel many times in the order of magnitude of about - 400 mV, thus e.g. in the range of - 320 mV to - 480 mV.
- the somewhat higher potential may be an indication of the passivation of the metallic surface, in particular with the anions which, with the cations dissolved out of the metallic surface, form a passivation layer.
- the redox potential of the depot substance in the undisturbed state is e.g.
- Anions are released from the depot substance by 100 mV, by 150 mV, by 200 mV, by 250 mV or by 300 mV, so that there is no pronounced softening or only limited softening or even no softening of the defect, and sometimes not or only to a limited extent to a greater reduction of oxygen and radical formation at the metal / coating interface and also not to ei ⁇ ner stronger oxidation or limited to oxidation of the exposed metallic surface (see Figure 1).
- FIG. 1 a shows a cross section through the metallic surface with a coating which is damaged by a deep scratch.
- the optionally conductive polymer-containing coating Ctg is deposited on the metallic substrate Me or on an intermediate layer not shown here, such as a pretreatment layer mediating adhesion.
- the interface G between Ctg and Me is completely or / and almost completely detached in the region a around the defect.
- the saddle point A indicates the frequently assumed approximate position of the delimbing front at the respective point in time of the potential measurement. From the scratch to the saddle point A of the potential curve, the interface is often completely or / and almost completely unbonded ("damaged point") Between points A and B there can be at least one leading front, for example, of oxygen reduction Point B reaches the "disturbed area". From the minimum distance b from the defect, that is from the point B, the interface is virtually undamaged. The points A and B usually move away from the defect over the course of time and thus increase the damaged area or the disturbed area, as the bold curve shows.
- the subfigures 1 b), 1 c) and 1 d) represent potential changes over time in the area from the defect to undisturbed coating in diagrams of the potential e over the distance d.
- the subfigures 1 b), 1 c) and 1 d) show the potential changes in the Delamina- tion of a coating of a same initial stage in all cases to a certain, somewhat advanced stage after a time .DELTA.t-i, in the softening the interface metal / coating in the subfigures 1 b) and 1 c) is already somewhat advanced.
- Partial figure 1 b shows a change in potential on a coating without release of anions.
- the potential reduction progresses further into the intact area to the side of the scratch.
- the potential curve occurring after the time .DELTA.t.sub.i is substantially similar to the curve of the initial stage, with the corrosion potential of the defect already being set in the area already released, but possibly also a slight or greater potential increase in this area being observed. which is then due to an ohmic voltage drop, which is not completely due to the ion transport along the ent tied boundary G is conditional. In these cases, the potential drop P is reduced by a potential difference P 2 after the time ⁇ ti. 1
- the defect potential in the scratch practically does not change.
- Part 1 c) illustrates the potential change in the disturbed area when a depot substance is present and when a certain amount of anions that inhibit the anodic partial reaction of corrosion is released.
- the corrosion potential in the defect and the ohmic coupling increases to a certain extent even in the disturbed region.
- the potential drop P 1 in the disturbed region is reduced, and thus the driving force for the progression of the delamination also decreases. Even if it does not lead to complete passivation in the defect, this may already be sufficient to bring the progress of the delamination almost completely to a standstill or to substantially reduce the speed of this progression. However, a larger potential difference remains between the disturbed and the undisturbed area (corresponds to P 1 ).
- the subfigure 1 d) represents the approximately ideal case with a virtually complete passivation of the defect, in which the delamination completely comes to a standstill and also the potential difference between the disturbed and the undisturbed area (corresponding to P 1 ) is minimized.
- Sub-part 1 d) shows that after successful defect healing, the release of further anions from the depot substance is stopped, since the potential difference between the defect and the depot substance decreases to a minimum.
- the release mechanism according to the invention is self-regulating in the sense that it takes place only when necessary and does not run unchecked and that the further anions remain in the depot substance for use in the event of further damage.
- cathodic delamination such as iron / steel or mixed cathodic and anodic delamination such as on zinc / zinc alloys
- the progress of delamination primarily becomes due to the oxygen reduction rate and further to the stability of the metal / coating interface and adhesion at that interface certainly.
- These delamination types are determined by the oxygen driven reduction rate and the resulting radicals that destroy the Grenzflä ⁇ chenhaftung between metal and coating.
- Cathodic delamination is usually faster than anodic delamination. Therefore, the cathodic front of oxygen reduction on the anodic front of metal oxidation usually precedes and spreads faster and further around the defect.
- the dissolution of the metallic surface takes place at the anodic delamination front, that is to say at the anodic front, for example the metal dissolution.
- This is coupled with incipient softening and a potential reduction. It occurs in particular during filiform corrosion. In all cases, however, there is a drop in potential at the anodic or cathodic front.
- the leading front may in particular comprise a cathodic front, e.g. This can be coupled with the initial delamination and with a potential reduction.
- the cathodic front often occurs, e.g. in iron, steels, zinc and zinc alloys.
- the object is further achieved by a method for protecting a metallic surface with a coating of a corrosion-inhibiting composition, in which a coating is applied to the metallic surface, which is optionally dried after application and optionally also cured, which is used as component ( n) a) at least one depot substance and optionally b) contains at least one further component or / and at least one matrix substance, in particular conductive polymer, wherein at least one kind of anions is selected according to that these ions in water, in at least one other are polar solvent or / and in a mixture containing at least one non-polar solvent be ⁇ movable, wherein at least one starting material for the preparation of the depot substance (s) is selected thereafter that its oxidation potential is less than or equal to the decomposition potential of the water or / and at least one other en polar solvent in the mixture used for this purpose, wherein at least one type of anti-corrosive and possibly also at least one type of adhesion-promoting anions can be built into at least one depot substance 1.
- the potential of the at least one depot substance can also be released again, and if it has a metallic surface, it can have an anticorrosive effect
- at least one depot substance has a redox potential which prevents premature release of at least one type of anticorrosive and optionally also at least one type of adhesion-promoting anions ermög ⁇ light
- the release of at least one kind of anti-corrosive and ge ⁇ possibly also of at least one kind of adhesion-promoting anions from at least one depot substance not or / and only subordinate via a deprotonation reaction, but predominantly or / and entirely by way of a reduction reaction
- at least one depot substance has such pore sizes that the selected anti-corrosive and / or adhesion-promoting anions to be released do not or do not substantially migrate through the at least one depot substance and optionally through at least one further Component
- the cation transport rate of the cations from the electrolyte, in particular from the defect or / and from the metallic surface, into the at least one depot substance is preferably less than 10 -8 cm 2 / s, more preferably less than 10 -10 cm 2 / s, very particularly preferably less than 10 ⁇ 12 cm 2 / s, in particular less than 10 "14 cm 2 / s.
- the redox properties of the conductive polymer are preferably to be set such that a sufficiently high release of the anions takes place even at a slight reduction of the potential at the interface, so that anions already become active at the very front of the delamination in order to be effective To be able to counteract the training of a significant damage to the further damage.
- a response as early as possible to the impending or already beginning corrosive attack can already begin.
- the delamination rate can be greatly increased around the damaged site and, in the critical case, also far beyond this site if passivation of the defect, for example due to an excessive defect area, is unsuccessful. If the cation transport rate of the cations from the electrolyte, in particular from the defect and / or the metallic surface, is kept comparatively low, it is prevented that the chemical system collapses prematurely or can even collapse.
- the amount of at least one depot substance or of the at least one depot substance is preferably distributed as homogeneously as possible in at least one matrix substance or substantially homogeneously distributed and selected such that a sufficiently high release of the anions occurs that the anion transport rate in the coating sufficient to defect in order to achieve a delamination-inhibiting effect, but possibly also so that, on the other hand, the cation transport rate is kept so low that it does not or not substantially promotes the Delami- nation.
- the too high cation transport rate for cations from the electrolyte or / and from the defect leads to a continuous reduction of the depot substance and, consequently, to an increase in the lead ion concentration at the interface and therefore the ka ⁇ thodische delamination is greatly accelerated.
- the depot substance can also be continuously reduced.
- the size of the anion transport rate in the coating to the defect is also dependent on the potential gradient and also dependent on the type of metallic surface and its corrosion potential. It is preferably in each case at approximately 10 -5, 10 -6, 10 "7 10" 8 or 10 -9 cm 2 / s, often at about 10 "10, 10 or 10 '11 ⁇ 12 cm 2 / s.
- the anion transport rate can be influenced by selecting as small anions as possible, which emigrate well from the depot substance and can migrate through the coating of matrix and components, and that an adequate number and size of the pore channels or structural pores in the depot substance, if appropriate in their matrix and / or, if appropriate, in the other components of the coating for the migrating anions, in order to prepare the anionic anion. portrate not or not significantly affect.
- the migration behavior may possibly also be influenced by the fact that 1. Matrix substances are selected such that pores or channels form on the discharge of solvent (s) and / or volatile components from the applied and drying coating, in that 2 matrix substances are selected.
- a component is used to control the water absorption capacity of at least one matrix substance or / and at least one component, for example a water-soluble polymer such as polyacrylic acid.
- a more or less loose pore or channel structure can be achieved, in particular, by a mixture in which only a part of the polymer particles is plasticized and / or in which partially plasticized polymer particles are present.
- an addition of, for example, at least one compound based on polyacrylic acid or / and of polyvinyl alcohol can serve to increase the water absorption capacity and ensure a ventilation effect and larger pore spaces in the dry film.
- the pores or pore channels may also be present in this case or only in the nanometer range or even or only cavities may be approximately in the molecular scale.
- the cation transport rate of the coating can be adjusted by selecting the content of depot substance and thus the amount of incorporated and releasable anions such that the lowest possible cation transport rate results in damage to the coating and in the release of the anions.
- the cation transport rate is then preferably approximately 10 "8 10" 9, 10 "10, 10" 11, 10 '12 '13 10 or 10 "14 cm 2 / s.
- For a large defect is a greater amount of de- Potent substance and thus on built-in and releasable anions required. It is expected that the corrosion on small defects such as scratches were ⁇ inhibited was ⁇ can, but large-scale defects are likely not inhi ⁇ biert many times.
- the inhibitable defect size is also dependent on the thickness of the coating and can be estimated by the ratio of the interface as the edge of the coating to the defect area of the exposed individual defect. For small defects, this ratio often has values in the range of about 0.01 to 100 or 1000, while large defects with a ratio of eg 10,000 or greater can no longer be inhibited, as in chromating.
- Oxygen reduction produces radicals or anions such as OH ' , O 2 " , etc., which can destroy the adhesion at the metal / coating interface: this can quickly lead to complete softening, which can be counteracted by: 1.) by releasing anions which markedly reduce the oxygen reduction at the metal / coating interface, 2) by causing a substantial or complete release of the anions from the depot substance, thereby keeping the cation transport rates of the cations, in particular from the electrolyte and / or from the defect, to a minimum or can be significantly reduced, whereby the charge transport necessary for maintaining the cathodic partial reaction is also kept small, which also counteracts the formation of radicals in the region of the metal / coating interface, 3.) by the radical formation per interface unit the shift of oxygen reduction from the G metal surface / coating is displaced to the interface between two superimposed coatings or / and 4.) on the one hand, at least one radical scavenger is incorporated into the coating containing the depot substance. This third process is promoted by electronically
- the oxygen reduction can also be used in the process according to the invention for the oxygen reduction to be carried out in the case of at least two superimposed coatings. Because of the electronic conductivity of the depot substance to the interface between the two coatings, the oxygen reduction preferably takes place at the interface or boundary layer between the two adjoining coatings and less or not at the interface occurs between the metal and the first coating and so that the delamination occurs at the interface between the metal and the first coating less or not at all.
- the delamination can be slowed down or stopped by the addition of radical scavengers.
- the liberation and migration of the anions from the conductive polymer to the corrosive region and the desired corrosion-protective effect of the coatings according to the invention were achieved not only in very specific experiments, such as with a scanning Kelvin probe (SKP), but enrichment of the Released corrosion-protecting anions in the corrosive area and a significant increase in the corrosion protection of metallic substrates with ei ⁇ ner organic coating containing conductive polymer, also in makroskopi ⁇ rule area with practice-relevant samples and tests such as salt spray test prove.
- SSP scanning Kelvin probe
- Sulphate is an anion that can basically be removed from the depot substance, but neither acts to inhibit corrosion nor acts as an adhesion promoter.
- a large-area defect was applied on the coated surface, which was sufficient for the metal.
- a 0.1-molar sodium chloride solution was applied to this large-area defect, which touched the coated area only at the edge of the defect.
- FIG. 3 (Comparative Example 1) shows the change over time of the potential curve from curve to curve, in each case at intervals of 2 hours.
- the disturbed area is spreading continuously.
- a strong weakening of the propagation velocity over time and a significant change in the corrosion potential in the defect are not recognizable.
- FIG. 2 shows the change with time of the potential curve from curve to curve at intervals of 2 hours with the release of corrosion-inhibiting anions, as already reproduced by way of example in FIG. 1 c).
- the corrosion potential in the disturbed region initially rises sharply and then slightly further, as a result of which the potential difference between the undisturbed region and the disturbed region is markedly reduced, and thus the driving force for the propagation of the delamination is also markedly reduced.
- the propagation speed of the disturbed area decreases until the propagation speed becomes almost zero after several hours. Already this not complete passivation leads to an almost complete stoppage of the delamination.
- Example 2 In analogy to Example 1, in Example 2, the protective effect is achieved by the liberated molybdate anions, which can inhibit the corrosion in the defect. Since in Example 2, due to the complete immersion of the sample in the corrosive solution, the ratio of the volume or area of active depot substance to the area of the defect in the scratch is orders of magnitude more favorable than in Example 1 (delamination in one only locally in the defect and on the defect rim acting corrosive solution), the protective effect observed here is also more obvious.
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Applications Claiming Priority (5)
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DE200410037542 DE102004037542A1 (de) | 2004-08-03 | 2004-08-03 | Verfahren zum Schützen einer metallischen Oberfläche mit einer korrosionsinhibierenden Beschichtung |
DE102004037552 | 2004-08-03 | ||
DE200510030489 DE102005030489B4 (de) | 2005-06-30 | 2005-06-30 | Verfahren zum Beschichten von Partikeln mit leitfähigen Polymeren, Gemisch zum Beschichten, beschichtete Partikel, die Verwendung derart beschichteter Partikel und Zusammensetzung einer Beschichtung |
DE200510030488 DE102005030488A1 (de) | 2005-06-30 | 2005-06-30 | Verfahren zum Beschichten metallischer Oberflächen mit einer korrosionsschützenden Beschichtung |
PCT/EP2005/008306 WO2006015754A2 (de) | 2004-08-03 | 2005-08-01 | Verfahren zum schützen einer metallischen oberfläche mit einer korrosionsinhibierenden beschichtung |
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EP05773771.0A Not-in-force EP1778413B1 (de) | 2004-08-03 | 2005-08-01 | Verfahren zum beschichten metallischer oberflächen mit einer korrosionsschützenden beschichtung |
EP20050768365 Not-in-force EP1779392B1 (de) | 2004-08-03 | 2005-08-03 | Verfahren zum beschichten von feinen partikeln mit leitfähigen polymeren |
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EP20050768365 Not-in-force EP1779392B1 (de) | 2004-08-03 | 2005-08-03 | Verfahren zum beschichten von feinen partikeln mit leitfähigen polymeren |
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JP (3) | JP2008508429A (pl) |
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CN106519988A (zh) * | 2016-10-28 | 2017-03-22 | 昆山聚贝机械设计有限公司 | 一种机械设备用环保型防锈抛光液 |
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RU2357003C2 (ru) * | 2003-02-25 | 2009-05-27 | Шеметалл Гмбх | Способ нанесения покрытий на металлические поверхности смесью, содержащей по крайней мере два силана |
WO2005069892A2 (en) * | 2004-01-16 | 2005-08-04 | Battelle Memorial Institute | Methods and apparatus for producing ferrate(vi) |
WO2006015756A1 (de) * | 2004-08-03 | 2006-02-16 | Chemetall Gmbh | Verfahren zum beschichten metallischer oberflächen mit einer korrosionsschützenden beschichtung |
EP1812621B1 (de) * | 2004-11-10 | 2019-03-06 | Chemetall GmbH | Verfahren zur beschichtung von metallischen oberflächen mit einer wässerigen silan/ silanol/ siloxan/ polysiloxan enthaltenden zusammensetzung |
US8101014B2 (en) * | 2004-11-10 | 2012-01-24 | Chemetall Gmbh | Process for coating metallic surfaces with a multicomponent aqueous composition |
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2005
- 2005-08-01 WO PCT/EP2005/008309 patent/WO2006015756A1/de active Application Filing
- 2005-08-01 JP JP2007524254A patent/JP2008508429A/ja active Pending
- 2005-08-01 BR BRPI0513094-8A patent/BRPI0513094A/pt not_active IP Right Cessation
- 2005-08-01 ES ES05773771T patent/ES2570986T3/es active Active
- 2005-08-01 CA CA 2576253 patent/CA2576253A1/en not_active Abandoned
- 2005-08-01 WO PCT/EP2005/008306 patent/WO2006015754A2/de active Application Filing
- 2005-08-01 MX MX2007001362A patent/MX2007001362A/es active IP Right Grant
- 2005-08-01 EP EP05769621A patent/EP1776196A2/de not_active Ceased
- 2005-08-01 MX MX2007001376A patent/MX2007001376A/es not_active Application Discontinuation
- 2005-08-01 BR BRPI0513098-0A patent/BRPI0513098A/pt not_active IP Right Cessation
- 2005-08-01 JP JP2007524255A patent/JP2008508097A/ja active Pending
- 2005-08-01 US US11/659,165 patent/US20080305341A1/en not_active Abandoned
- 2005-08-01 CA CA 2575885 patent/CA2575885A1/en not_active Abandoned
- 2005-08-01 EP EP05773771.0A patent/EP1778413B1/de not_active Not-in-force
- 2005-08-01 US US11/659,156 patent/US20080171211A1/en not_active Abandoned
- 2005-08-03 MX MX2007001361A patent/MX2007001361A/es unknown
- 2005-08-03 EP EP20050768365 patent/EP1779392B1/de not_active Not-in-force
- 2005-08-03 CA CA 2575927 patent/CA2575927A1/en not_active Abandoned
- 2005-08-03 BR BRPI0513088-3A patent/BRPI0513088A/pt not_active IP Right Cessation
- 2005-08-03 WO PCT/EP2005/008314 patent/WO2006015757A1/de active Application Filing
- 2005-08-03 US US11/659,141 patent/US20080175992A1/en not_active Abandoned
- 2005-08-03 JP JP2007524258A patent/JP2008508411A/ja not_active Withdrawn
-
2011
- 2011-10-20 US US13/277,510 patent/US20120052307A1/en not_active Abandoned
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2012
- 2012-04-04 US US13/439,174 patent/US20120208086A1/en not_active Abandoned
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106519988A (zh) * | 2016-10-28 | 2017-03-22 | 昆山聚贝机械设计有限公司 | 一种机械设备用环保型防锈抛光液 |
Also Published As
Publication number | Publication date |
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EP1779392A1 (de) | 2007-05-02 |
US20080171211A1 (en) | 2008-07-17 |
JP2008508429A (ja) | 2008-03-21 |
US20080175992A1 (en) | 2008-07-24 |
CA2575885A1 (en) | 2006-02-16 |
US20120208086A1 (en) | 2012-08-16 |
WO2006015754A2 (de) | 2006-02-16 |
MX2007001361A (es) | 2007-07-04 |
EP1778413B1 (de) | 2016-03-16 |
JP2008508411A (ja) | 2008-03-21 |
CA2576253A1 (en) | 2006-02-16 |
JP2008508097A (ja) | 2008-03-21 |
ES2570986T3 (es) | 2016-05-23 |
MX2007001362A (es) | 2007-04-16 |
CA2575927A1 (en) | 2006-02-16 |
EP1779392B1 (de) | 2012-06-13 |
WO2006015757A1 (de) | 2006-02-16 |
WO2006015754A3 (de) | 2006-03-16 |
BRPI0513098A (pt) | 2008-04-29 |
MX2007001376A (es) | 2007-04-10 |
BRPI0513094A (pt) | 2008-04-29 |
US20120052307A1 (en) | 2012-03-01 |
US20080305341A1 (en) | 2008-12-11 |
BRPI0513088A (pt) | 2008-04-29 |
EP1778413A1 (de) | 2007-05-02 |
WO2006015756A1 (de) | 2006-02-16 |
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