Classifications

• • 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
  • C23C—COATING 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
  • C23C22/00—Chemical 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
  • C23C22/05—Chemical 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
  • C23C22/06—Chemical 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
  • C23C22/34—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
• • 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
  • C23C—COATING 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
  • C23C22/00—Chemical 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
  • C23C22/05—Chemical 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
  • C23C22/06—Chemical 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
  • C23C22/48—Chemical 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 not containing phosphates, hexavalent chromium compounds, fluorides or complex fluorides, molybdates, tungstates, vanadates or oxalates
• • 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
  • C23C—COATING 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
  • C23C22/00—Chemical 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
  • C23C22/86—Regeneration of coating baths

Definitions

• the present invention relates to replenishing compositions and methods of replenishing pretreatment compositions.
• the present invention is directed to a method of replenishing a pretreatment composition comprising adding a replenisher composition to the pretreatment composition, wherein the replenisher composition comprises a zirconium complex.
• any numerical range recited herein is intended to include all sub-ranges subsumed therein.
• a range of "1 to 10" is intended to include all sub-ranges between (and including) the recited minimum value of 1 and the recited maximum value of 10, that is, having a minimum value equal to or greater than 1 and a maximum value of equal to or less than 10.
• substantially free means that a composition comprises ⁇ 1 weight percent, such as ⁇ 0.8 weight percent or ⁇ 0.5 weight percent or ⁇ 0.05 weight percent or ⁇ 0.005 weight percent, of a particular material (e.g., organic solvent, filler, etc.) based on the total weight of the composition.
• a particular material e.g., organic solvent, filler, etc.
• completely free means that a composition does not comprise a particular material (e.g., organic solvent, filler, etc.). That is, the composition comprises 0 weight percent of such material.
• metal ions and metals referred to herein are those elements included in such designated group of the CAS Periodic Table of the Elements as is shown, for example, in the Handbook of Chemistry and Physics, 68th edition (1987).
• replenisher composition refers to a material added to a pretreatment composition during the pretreatment process.
• the replenisher composition does not have the same formulation as the pretreatment composition although certain components of the formulation may be the same.
• the replenisher composition may comprise components which the pretreatment composition lacks.
• the pretreatment composition of the present invention may comprise H 2 ZrF 6
• the replenisher composition of the present invention comprises a zirconium complex that may not have been present in the original formulation of the pretreatment composition as well as optionally comprising H 2 ZrF 6 .
• the present invention is not directed to simply adding more pretreatment composition to a pretreatment bath, which comprises the pretreatment composition, in order to replenish the bath. Rather, it is directed to adding a replenisher composition to a pretreatment composition wherein the replenisher composition has a different formulation from that of the pretreatment composition.
• the pretreatment composition may include one or more components of a pretreatment bath.
• the replenisher composition of certain methods of the present invention comprises (a) a zirconium complex.
• a zirconium complex for the purposes of the present invention, is defined as a zirconium compound that is not an oxide, hydroxide, or carbonate of zirconium.
• Suitable zirconium complex compounds include zirconium compound of a sulfonic acid such as zirconium methanesulphonic acid.
• the replenisher composition may, optionally, further comprise (b) a dissolved complex metal fluoride ion, wherein the metal ion comprises a Group IIIA metal, Group IVA metal, Group IVB metal, or combinations thereof.
• the metal can be provided in ionic form, which can be easily dissolved in an aqueous composition at an appropriate pH, as would be recognized by those skilled in the art.
• the metal may be provided by the addition of specific compounds of the metals, such as their soluble acids and salts.
• the metal ion of the dissolved complex metal fluoride ion (b) is capable of converting to a metal oxide upon application to a metal substrate.
• the metal ion of dissolved complex metal fluoride ion comprises silicon, germanium, tin, boron, aluminum, gallium, indium, thallium, titanium, zirconium, hafnium, or combinations thereof.
• a source of fluoride ion is also included in the dissolved complex metal fluoride ion (b) to maintain solubility of the metal ions in solution.
• the fluoride may be added as an acid or as a fluoride salt. Suitable examples include, but are not limited to, ammonium fluoride, ammonium bifluoride, hydrofluoric acid, and the like.
• the dissolved complex metal fluoride ion (b) is provided as a fluoride acid or salt of the metal.
• the dissolved complex fluoride ion (b) provides both a metal as well as a source of fluoride to the replenisher composition.
• Suitable examples include, but are not limited to, fluorosilicic acid, fluorozirconic acid, fluorotitanic acid, ammonium and alkali metal fluorosilicates, fluorozirconates, fluorotitanates, zirconium fluoride, sodium fluoride, sodium bifluoride, potassium fluoride, potassium bifluoride, and the like.
• the dissolved complex metal fluoride ion component [0018] In certain embodiments, the dissolved complex metal fluoride ion component
• (b) of the replenisher composition comprises H 2 TiF 6 , H 2 ZrF 6 , ⁇ 2 ⁇ 13 ⁇ 4, H 2 SiF 6 , H 2 GeF 6 , H 2 SnF 6 , or combinations thereof.
• the dissolved complex metal fluoride ion component [0019] In certain embodiments, the dissolved complex metal fluoride ion component
• (b) of the replenisher composition is present in the replenisher composition in an amount ranging from 1 to 25 percent by weight metal ions, based on the weight of total metal ions of the replenisher composition.
• the dissolved complex metal fluoride ion component of the replenisher composition is present in the replenisher composition in an amount ranging from 1 to 15 percent by weight metal ions, such as from 2 to 10 percent by weight metal ions, based on the weight of total metal ions of the replenisher composition.
• the replenisher composition may, optionally, further comprise (c) a component comprising an oxide, hydroxide, or carbonate of Group IIIA, Group IVA, Group IVB metals, or combinations thereof.
• Suitable examples of Group IIIA, Group IVA, Group IVB metals of component (c) include, but are not limited to, aluminum, gallium, indium, thallium, silicon, germanium, tin, lead, titanium, zirconium, hafnium, and the like.
• the metal ion of component (c) comprises titanium, zirconium, hafnium, aluminum, silicon, germanium, tin, or combinations thereof.
• component (c) comprises zirconium basic carbonate, aluminum hydroxide, tin oxide, silicon hydroxide, or combinations thereof.
• component (c) comprises a zirconyl compound.
• a zirconyl compound, as defined herein, refers to a chemical compound containing a zirconyl group (ZrO).
• the zirconyl compound in the pretreatment composition comprises zirconyl nitrate (ZrO(N03) 2 ), zirconyl acetate (ZrO(C 2 H 3 0 2 ) 2 , zirconyl carbonate (ZrOCOs), protonated zirconium basic carbonate (Zr 2 (OH) 2 C0 3 ), zirconyl sulfate (ZrOS0 4 ) 2 , zirconyl chloride (ZrO(Cl) 2 , zirconyl iodide (ZrO(I) 2 , zirconyl bromide (ZrO(Br) 2 , or a mixture thereof.
• the replenisher composition of the present invention in certain of the embodiments, is added to the pretreatment composition to maintain the metal ion content in the pretreatment composition to between 10 ppm ("parts per million") to 250 ppm metal ions (measured as elemental metal), such as from 30 ppm to 200 ppm metal ions, such as from 150 (150) ppm to 200 ppm metal ions in the pretreatment composition.
• the metal ion content as defined herein, is the total metal ions contributed from the zirconium complex (a), the optional components (b) and/or (c), when present, in addition to the metal ions in the pretreatment composition not contributed by the replenishing composition.
• the total amount of replenisher composition comprising the zirconium complex (a) that is added to the pretreatment composition is such that the total metal ion content in the replenished bath contributed from both the zirconium complex (a) and the remaining metal ions from the pretreatment composition is between 10 ppm ("parts per million") to 250 ppm metal ions (measured as elemental metal), such as from 30 ppm to 200 ppm metal ions, such as from 150 (150) ppm to 200 ppm metal ions in the pretreatment composition.
• the total amount of replenisher composition added to the pretreatment composition is such that the total metal ion content in the replenished bath contributed from the zirconium complex (a), components (b) and/or (c), and the remaining metal ions from the pretreatment composition is between 10 ppm ("parts per million") to 250 ppm metal ions (measured as elemental metal), such as from 30 ppm to 200 ppm metal ions, such as from 150 (150) ppm to 200 ppm metal ions in the pretreatment composition.
• the metal ion comprises zirconium. In other embodiments, the metal ion comprises zirconium in combination with another metal ion present in the replenisher composition, as discussed below.
• component (c) is present in the replenisher composition in an amount ranging from 8 to 90 percent by weight metal ions based on the weight of total metal ions of components (b) and (c) of the replenisher composition. In still other embodiments, component (c) is present in the replenisher composition in an amount ranging from 10 to 35 percent by weight metal ions based on the weight of total metal ions of components (b) and (c) of the replenisher composition.
• the replenisher composition may, optionally, further comprise (d) a dissolved metal ion comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal, Lanthanide Series metal, or combinations thereof.
• component (d) comprises manganese, cerium, cobalt, copper, zinc, iron, or combinations thereof.
• Water-soluble forms of metals can be utilized as a source of the metal ions comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal, and/or Lanthanide Series metal.
• Suitable compounds include, but are not limited to, ferrous phosphate, ferrous nitrate, ferrous sulfate, copper nitrate, copper sulfate, copper chloride, copper sulfamate, zinc nitrate, zinc sulfate, zinc chloride, zinc sulfamate, and the like.
• component (d) is present in the replenisher composition at a weight ratio of 1 :10 to 10: 1 based on the weight of total metal ions of zirconium complex (a) to the weight of total metal ions comprising component (d). In other embodiments, the weight ratio is from 1:6 to 6:1, such as from 1 :4 to 4:1 based on the weight of total metal ions of zirconium complex (a) to the weight of total metal ions comprising component (d).
• the replenisher composition of the methods of the present invention is provided as an aqueous solution and/or dispersion. In these embodiments, the replenisher composition further comprises water. Water may be used to dilute the replenisher composition used in the methods of the present invention. Any appropriate amount of water may be present in the replenisher composition to provide the desired concentration of other ingredients.
• the pH of the replenisher composition may be adjusted to any desired value.
• the pH of the replenisher composition may be adjusted by varying the amount of the dissolved complex metal fluoride ion present in the composition.
• the pH of the replenisher composition may be adjusted using, for example, any acid or base as is necessary.
• the pH of the replenisher is maintained through the inclusion of a basic material, including water soluble and/or water dispersible bases, such as sodium hydroxide, sodium carbonate, potassium hydroxide, ammonium hydroxide, ammonia, and/or amines such as triethylamine, methylethyl amine, or combinations thereof.
• the pH of the replenisher may be adjusted by the addition of the zirconium complex (a), particularly by the addition of zirconium methanesulphonic acid, alone or in combination with the optional components (b), (c) and/or (d) described in the previous paragraph.
• the replenisher composition including any of those compositions set forth above, is added to the pretreatment composition in an amount sufficient to maintain the pH of the pretreatment composition at a pH of 6.0 or below. In still other embodiments, the replenisher composition is added to maintain the pH of the pretreatment composition at a level of from 4.0 to 6.0, such as from 4.5 to 5.5.
• the replenisher composition of the methods of the present invention is prepared by combining the zirconium complex (a) and water to form a first preblend.
• the ingredients of the first preblend may be agitated under mild agitation once the ingredients are combined with one another.
• component (b), (c) and/or (d) are present, these components (b), (c) and/or (d) and water may be combined to form a second, third and/or fourth preblend, respectively.
• the ingredients of the second preblend, third and/or fourth preblend may be agitated under mild agitation once the ingredients are combined with one another.
• the first preblend may then be added to the second, third and/or fourth preblend.
• the replenisher composition may be prepared at ambient conditions, such as approximately 70°F to 80°F (21 to 26 ° C), or at temperatures slightly below and/or slightly above ambient conditions, such as from approximately 50°F to 140°F (10 to 60 ° C).
• the replenisher composition may be added to the pretreatment composition under agitation. In other embodiments, the replenisher composition may be added to the pretreatment composition without agitation followed by agitation of the materials.
• the replenisher composition may be added to the pretreatment composition when the pretreatment composition is at ambient temperature, such as approximately 70°F to 80°F (21 to 26 ° C), as well as when the pretreatment composition is at temperatures slightly below and/or slightly above ambient temperature, such as, for example, from approximately 50°F to 140°F (10 to 60 ° C).
• the methods of the present invention are directed toward adding a replenisher composition to a pretreatment composition.
• pretreatment composition refers to a composition that upon contact with a substrate, reacts with and chemically alters the substrate surface and binds to it to form a protective layer.
• the pretreatment composition of the methods of the present invention comprises water and (i) a dissolved complex metal fluoride ion wherein the metal ion comprises a Group IIIA metal, Group IVA metal, Group IVB metal, Group VB metal or combinations thereof.
• the dissolved complex metal fluoride ion (i) of the pretreatment composition may be any of those described above related to the optional dissolved complex metal fluoride ion (b) of the replenisher composition.
• the dissolved complex metal fluoride ion (i) of the pretreatment composition is different from the optional dissolved complex metal fluoride ion (b) of the replenisher composition.
• the dissolved complex metal fluoride ion (i) of the pretreatment composition is the same as the optional dissolved complex metal fluoride ion (b) of the replenisher composition.
• the metal ion of the optional dissolved complex metal fluoride ion (b) of the pretreatment composition comprises titanium, zirconium, hafnium, silicon, germanium, tin, or combinations thereof.
• the dissolved complex metal fluoride ion of component (i) of the pretreatment composition comprises ]3 ⁇ 4TiF6, kZrFe, tHfFe, H 2 S1F6, ⁇ GeFe, ⁇ SnFe, or combinations thereof.
• the dissolved complex metal fluoride ion (i) is present in the pretreatment composition in an amount to provide a concentration of from 10 ppm ("parts per million") to 250 ppm metal ions (measured as elemental metal), such as from 30 ppm to 200 ppm metal ions, such as from 150 ppm to 200 ppm metal ions in the pretreatment composition.
• the pretreatment composition may, optionally, further comprise (ii) a dissolved metal ion comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal, Lanthanide Series metal, or combinations thereof.
• the dissolved metal ion (ii) of the pretreatment composition may be any of those described above related to the optional dissolved metal ion (d) of the replenisher composition.
• the dissolved metal ion (ii) of the pretreatment composition is different from the optional dissolved metal ion (d) of the replenisher composition.
• the dissolved metal ion (ii) of the pretreatment composition is the same as the optional dissolved metal ion (d) of the replenisher composition.
• the replenisher composition will comprise the optional dissolved metal ion of component (d).
• the pretreatment composition does not comprise the dissolved metal ion of component (ii)
• the replenisher composition may or may not comprise the optional dissolved metal ion of component (d).
• the dissolved metal ion (ii) of the pretreatment composition comprises manganese, cerium, cobalt, copper, zinc, or combinations thereof.
• Suitable compounds include, but are not limited to, ferrous phosphate, ferrous nitrate, ferrous sulfate, copper nitrate, copper sulfate, copper chloride, copper sulfamate, zinc nitrate, zinc sulfate, zinc chloride, zinc sulfamate, and the like.
• the dissolved metal ion (ii) is present in the pretreatment composition in an amount to provide a concentration of from 5 ppm to 200 ppm metal ions (measured as elemental metal), such as from 10 ppm to 100 ppm metal ions in the pretreatment composition.
• the pretreatment composition also comprises water. Water may be present in the pretreatment composition at any appropriate amount to provide the desired concentration of other ingredients.
• the pretreatment composition comprises materials which are present to adjust pH.
• the pH of the pretreatment composition ranges from 2.0 to 7.0, such as from 3.5 to 6.0.
• the pH of the pretreatment composition described here relates to the pH of the composition prior to contacting the pretreatment composition with a substrate during the pretreatment process.
• the pH of the pretreatment composition may be adjusted using, for example, any acid or base as is necessary.
• the pH of the pretreatment composition is maintained through inclusion of a basic material, including water soluble and/or water dispersible bases, such as sodium hydroxide, sodium carbonate, potassium hydroxide, ammonium hydroxide, ammonia, and/or amines such as triethylamine, methylethyl amine, or combinations thereof
• a basic material including water soluble and/or water dispersible bases, such as sodium hydroxide, sodium carbonate, potassium hydroxide, ammonium hydroxide, ammonia, and/or amines such as triethylamine, methylethyl amine, or combinations thereof
• the pretreatment composition may optionally contain other materials, including but not limited to nonionic surfactants, water dispersible organic solvents, defoamers, wetting agents, fillers, and resinous binders.
• the pretreatment composition is substantially free or, in some cases, completely free of any water dispersible organic solvents.
• Suitable resinous binders, as well as their weight percents, which may be used in connection with the pretreatment composition disclosed herein are described in U.S. Patent Application Pub. No. 2009/0032144A1, paragraph [0036] through paragraph [0038], the cited portion being incorporated herein by reference.
• Suitable fillers that may be used in connection with the pretreatment composition disclosed herein are described in U.S. Patent Application Pub. No. 2009/0032144A1, paragraph [0042], the cited portion being incorporated herein by reference.
• the pretreatment composition is substantially free or, in some cases, completely free of any filler.
• the pretreatment composition also comprises a reaction accelerator, such as nitrite ions, nitrate ions, nitro-group containing compounds, hydroxylamine sulfate, persulfate ions, sulfite ions, hyposulfite ions, peroxides, iron (III) ions, citric acid iron compounds, bromate ions, perchlorate ions, chlorate ions, chlorite ions as well as ascorbic acid, citric acid, tartaric acid, malonic acid, succinic acid and salts thereof.
• a reaction accelerator such as nitrite ions, nitrate ions, nitro-group containing compounds, hydroxylamine sulfate, persulfate ions, sulfite ions, hyposulfite ions, peroxides, iron (III) ions, citric acid iron compounds, bromate ions, perchlorate ions, chlorate ions, chlorite ions as well ascorbic acid, citric acid,
• the pretreatment composition is substantially free or, in some cases, completely free of a reaction accelerator.
• the pretreatment composition also comprises phosphate ions. Suitable materials and their amounts are described in U.S. Patent Application Pub. No. 2009/0032144A1 at paragraph [0043], incorporated herein by reference. In certain embodiments, however, the pretreatment composition is substantially or, in some cases, completely free of phosphate ion. As used herein, the term “substantially free” when used in reference to the absence of phosphate ion in the pretreatment composition, means that phosphate ion is present in the composition in an amount less than 10 ppm. As used herein, the term “completely free”, when used with reference to the absence of phosphate ions, means that there are no phosphate ions in the composition at all.
• the pretreatment composition is substantially or, in some cases, completely free of chromate and/or heavy metal phosphate, such as zinc phosphate.
• reaction products refers to soluble and/or insoluble substances that are formed during deposition of a pretreatment composition onto a substrate and from materials added to the pretreatment composition to control bath parameters, including the replenisher composition, and does not include the pretreatment film formed on the substrate. If any of these parameters fall outside of a desired concentration range, the effectiveness of depositing a metal compound onto a substrate can be impacted. For example, the pH of the pretreatment composition may decrease over time (e.g., become too acidic) which can impact the effectiveness of depositing metal compound onto the substrate.
• an increased concentration of reaction products present in a pretreatment composition can also interfere with proper formation of the pretreatment coating onto a substrate which can lead to poor properties, including corrosion resistance.
• fluoride ions associated with the metal compound can become dissociated from the metal compound and released into the pretreatment composition as free fluoride, and if left unchecked, will increase with time.
• free fluoride refers to isolated fluoride ions that are no longer complexed and/or chemically associated with a metal ion and/or hydrogen ion, but rather independently exist in the bath.
• total fluoride refers to the combined amount of free fluoride and fluoride that is complexed and/or chemically associated with a metal ion and/or hydrogen ion, i.e., fluoride which is not free fluoride.
• any suitable method for determining the concentration of free fluoride and total fluoride may be used, including for example, ion selective electrode analysis (ISE) using a calibrated meter capable of such measurements, such as an Accumet XR15 meter with an Orion Ionplus Sure-Flow Fluoride Combination electrode (available from Fisher Scientific).
• ISE ion selective electrode analysis
• the initial concentration of free fluoride of the pretreatment composition ranges from 10 to 200 ppm. In other embodiments, the initial concentration of free fluoride of the pretreatment composition ranges from 20 to 150 ppm.
• a pH controller may be added to the pretreatment composition in addition to the replenisher composition to achieve a desired pH.
• Any suitable pH controller commonly known in the art may be used, including for example, any acid or base as is necessary.
• Suitable acids include, but are not limited to, sulfuric acid and nitric acid.
• Suitable water soluble and/or water dispersible bases include, but are not limited to, sodium hydroxide, sodium carbonate, potassium hydroxide, ammonium hydroxide, ammonia, and/or amines such as triethylamine, methylethyl amine, or combinations thereof.
• a pH controller may be added to the pretreatment composition during the pretreatment process to adjust the pH of the pretreatment composition to a pH of 6.0 or below, such as a pH of 5.5 or below, such as a pH of 5.0 or below. In other embodiments, the pH controller may be added to adjust the pH to a level of from 4.0 to 5.0, such as from 4.6 to 4.8.
• the addition of the replenisher composition may maintain the pH of the pretreatment composition thereby reducing and/or eliminating the amount of pH controller that is added during the pretreatment process.
• addition of the replenisher composition results in addition of a pH controller at a lesser frequency during the pretreatment process. That is, addition of a pH controller to the pretreatment composition occurs a lesser number of times, compared to methods other than the present invention.
• addition of the replenisher composition results in a lesser amount of a pH controller that is added to the pretreatment composition during the pretreatment process compared to the amount of a pH controller that is added according to methods other than the methods of the present invention.
• the level of reaction product may be controlled through an overflow method, as would be recognized by those skilled in the art, in addition to the addition of the replenisher composition.
• a reaction product scavenger may be added to the pretreatment composition in addition to the replenisher composition.
• a "reaction product scavenger” refers to a material that, when added to a pretreatment composition during the pretreatment process, complexes with reaction products, for example free fluoride, present in the pretreatment composition, to remove the reaction products from the composition. Any suitable reaction product scavenger commonly known in the art may be used. Suitable reaction product scavengers include, but are not limited to, those described in U.S. Patent Application Pub. No. 2009/0032144A1, paragraphs [0032] through [0034], incorporated herein by reference.
• the addition of the replenisher composition may result in lower concentrations of reaction products during the pretreatment process thereby reducing and/or eliminating the amount of a reaction product scavenger that is added to a pretreatment composition during the pretreatment process.
• concentration of reaction products is lower as a result of addition of the replenisher composition, the level of sludge which may build during the pretreatment process is reduced and/or eliminated, although the inventors do not wish to be bound by any particular theory.
• addition of the replenisher composition results in addition of a reaction product scavenger at a lesser frequency during the pretreatment process. That is, addition of a reaction product scavenger to the pretreatment composition occurs a lesser number of times, compared to methods other than the methods of the present invention. In other embodiments, addition of the replenisher composition results in a lesser amount of a reaction product scavenger that is added to the pretreatment composition during the pretreatment process compared to the amount of a reaction product scavenger that is added according to methods other than the methods of the present invention.
• the present invention is directed toward a method of replenishing a pretreatment composition
• a replenisher composition comprising: (I) adding a replenisher composition to the pretreatment composition, wherein the replenisher composition comprises (a) a zirconium complex and may, optionally, further comprise one or more of (b) a dissolved complex metal fluoride ion wherein the metal ion comprises a Group IIIA metal, Group IVA metal, Group IVB metal, or combinations thereof; (c) a component comprising an oxide, hydroxide, or carbonate of Group IIIA, Group IVA, Group IVB metals or combinations thereof; and (d) a dissolved metal ion comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal, Lanthanide Series metal, or combinations thereof; and wherein the pretreatment composition comprises: (i) a dissolved metal ion comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal, Lanthanide Series metal, or combinations thereof; (ii)
• the present invention is directed toward a method of replenishing a pretreatment composition
• a method of replenishing a pretreatment composition comprising: (I) adding a replenisher composition to the pretreatment composition, wherein the replenisher composition comprises a) a zirconium complex and may, optionally, further comprise one or more of (b) a dissolved complex metal fluoride ion wherein the metal ion comprises a Group IIIA metal, Group IVA metal, Group IVB metal, or combinations thereof; (c) a component comprising an oxide, hydroxide, or carbonate of Group IIIA, Group IVA, Group IVB metals or combinations thereof; and (d) a dissolved metal ion comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal, Lanthanide Series metal, or combinations thereof; and wherein the pretreatment composition comprises: (i) a dissolved metal ion comprising a Group IB metal, Group IIB metal, Group VIIB metal, Group VIII metal; a Lanthanide Series metal, or
• the pretreatment composition replenished by the replenisher composition according to the methods of the present invention may be applied to a metal substrate.
• Suitable metal substrates for use in the present invention include those that are often used in the assembly of automotive bodies, automotive parts, and other articles, such as small metal parts, including fasteners, i.e., nuts, bolts, screws, pins, nails, clips, buttons, and the like.
• Specific examples of suitable metal substrates include, but are not limited to, cold rolled steel, hot rolled steel, steel coated with zinc metal, zinc compounds, or zinc alloys, such as electrogalvanized steel, hot-dipped galvanized steel, galvannealed steel, and steel plated with zinc alloy.
• metal substrate may be a cut edge of a substrate that is otherwise treated and/or coated over the rest of its surface.
• the metal substrate may be in the form of, for example, a sheet of metal or a fabricated part.
• the substrate may first be cleaned to remove grease, dirt, or other extraneous matter. This is often done by employing mild or strong alkaline cleaners, such as are commercially available and conventionally used in metal pretreatment processes.
• alkaline cleaners suitable for use in the present invention include CHEMKLEEN 163, CHEMKLEEN 177, and CHEMKLEEN 490MX, each of which are commercially available from PPG Industries, Inc. Such cleaners are often followed and/or preceded by a water rinse.
• the pretreatment composition replenished according to the methods of the present invention may be brought into contact with the substrate by any of known techniques, such as dipping or immersion, spraying, intermittent spraying, dipping followed by spraying, spraying followed by dipping, brushing, or roll-coating.
• the pretreatment composition when applied to the metal substrate is at a temperature ranging from 50 to 150 ° F (10 to 65 ° C).
• the contact time is often from 10 seconds to five minutes, such as 30 seconds to 2 minutes.
• the applied metal ion of the pretreatment coating composition generally ranges from 1 to 1000 milligrams per square meter (mg/m 2 ), such as 10 to 400 mg/m 2 .
• the thickness of the pretreatment coating can vary, but it is generally very thin, often having a thickness of less than 1 micrometer, in some cases it is from 1 to 500 nanometers, and, in yet other cases, it is 10 to 300 nanometers.
• the substrate may be rinsed with water and dried.
• the substrate is contacted with the pretreatment composition which has been replenished according to the methods of the present invention, it is then contacted with a coating composition comprising a film-forming resin.
• a coating composition comprising a film-forming resin.
• Any suitable technique may be used to contact the substrate with such a coating composition, including, for example, brushing, dipping, flow coating, spraying and the like.
• such contacting comprises an electrocoating step wherein an electrodepositable composition is deposited onto the metal substrate by electrodeposition.
• film-forming resin refers to resins that can form a self-supporting continuous film on at least a horizontal surface of a substrate upon removal of any diluents or carriers present in the composition or upon curing at ambient or elevated temperature.
• Conventional film-forming resins that may be used include, without limitation, those typically used in automotive OEM coating compositions, automotive refinish coating compositions, industrial coating compositions, architectural coating compositions, coil coating compositions, and aerospace coating compositions, among others.
• the coating composition comprises a thermosetting film-forming resin.
• thermosetting refers to resins that "set” irreversibly upon curing or crosslinking, wherein the polymer chains of the polymeric components are joined together by covalent bonds. This property is usually associated with a cross-linking reaction of the composition constituents often induced, for example, by heat or radiation. Curing or crosslinking reactions also may be carried out under ambient conditions. Once cured or crosslinked, a thermosetting resin will not melt upon the application of heat and is insoluble in solvents.
• the coating composition comprises a thermoplastic film-forming resin.
• thermoplastic refers to resins that comprise polymeric components that are not joined by covalent bonds and thereby can undergo liquid flow upon heating and are soluble in solvents.
• the substrate may be contacted with a coating composition comprising a film-forming resin by an electrocoating step wherein an electrodepositable coating is deposited onto the metal substrate by electrodeposition.
• Suitable electrodepositable coating compositions include those described in U.S. Patent Application Pub. No. 2009/0032144A1, paragraph [0051] through paragraph [0082], the cited portion of which being incorporated herein by reference.
• a replenisher composition was prepared as follows. The amount of each of the ingredients present in the replenisher composition of Example 1 is reflected in Table 1 below. Each of the percentages is expressed by weight.
• CHEMKLEEN 171 A alkaline cleaning product commercially available from PPG Industries, Inc.
• a fresh zirconium pretreatment bath was prepared using 0.88 grams per liter of hexafluorozirconic acid (45%) and 1.08 grams per liter of a copper nitrate solution (concentration 2% copper by weight). The remainder of the bath was deionized water. The pH of the bath was adjusted to approximately 4.5 with CHEMFIL BUFFER.
• the level of zirconium was measured by x-rite fluorescence.
• the initial zirconium level of the bath to be replenished with ZIRCOBOND Rl was approximately 187 ppm (measured as elemental metal).
• the initial zirconium level of the bath to be replenished with the replenisher composition of Example 1 was approximately 183 ppm (measured as elemental metal).
• the initial free fluoride of each of the baths was measured by ion selective electrode (ISE) analysis using a calibrated Accumet XR15 meter with an Orion Ionplus Sure- Flow Fluoride Combination electrode (model # 960900) (available from Fisher Scientific) using the following method.
• the meter was calibrated using fluoride calibration standards mixed with a buffer which were prepared as follows: fifty (50) milliliters of 10% trisodium citrate buffer solution was added to each two (2) milliliter sample of 100 mg/L, 300 mg/L and 1,000 mg/L fluoride standard.
• Panels were prepared for processing through the baths as follows. The panels were cleaned for two (2) minutes by spray application in a 2% v/v solution of CHEMKLEEN 166HP with 0.2% CHEMKLEEN 171A added. The panels were rinsed by immersing for approximately ten (10) seconds into deionized water, followed by an approximately ten (10) second spray with deionized water.
• a group of twenty (20) 4 x 6" panels were processed through each bath, the selection of panels consisted of: one (1) panel of aluminum (6111 T43); one (1) panel of cold rolled steel; two (2) hot dipped galvanized steel panels; and sixteen (16) electrogalvanized steel panels.
• the panels were immersed into the pretreatment bath for two (2) minutes at approximately 80°F (28°C), with mild agitation. Next, the panels were rinsed with an approximately 10 - 15 second spray with deionized water, and dried with a warm air blow- off.
• each of the pretreatment baths was measured for zirconium level, pH, and fluoride level using the methods described above.
• ZIRCOBOND Rl and the replenisher composition of Example 1 was added to each respective bath to adjust the zirconium level of the bath back to the starting value. Adjustments to bring the pH within the range of 4.4 - 4.8 and free fluoride level within the range of from 40-70 ppm were also made, if any adjustment was necessary. The pH was adjusted (if necessary) by adding CHEMFIL BUFFER to each of the baths. Free fluoride was adjusted (if necessary) by adding ZIRCOBOND CONTROL #4 to each of the baths.
• a replenisher composition was prepared as follows. The amount of each of the ingredients present in the replenisher composition of Example 1 is reflected in Table 1 below. Each of the percentages is expressed by weight. The amount of methanesulfonic acid present is enough to give a stoichiometric ratio of 4: 1 to the zirconium provided by the zirconium basic carbonate. TABLE 3
• ZIRCOBOND ZRF a zirconium pretreatment make-up product commercially available from PPG Industries, Inc.
• CHEMKLEEN 2010LP alkaline cleaning product commercially available from PPG Industries, Inc.
• a fresh zirconium pretreatment bath was prepared using 10.04 grams per liter of ZIRCOBOND ZRF in deionized water. The pH of the bath was adjusted to approximately 4.5 with CHEMFIL BUFFER.
• a four liter aliquot of the pretreatment bath was tested as follows: Panels were pretreated in the pretreatment bath to deplete it, as in Example 1, and then the bath was adjusted using the replenisher described in Table 2.
• the initial levels of zirconium and free fluoride were measured in the bath as described in Example 1.
• the level of zirconium was measured at 186 ppm (measured as elemental metal.
• the initial free fluoride was measured at 128 ppm.
• Example 1 as follows. The panels were cleaned for two (2) minutes by spray application in a 1.25% v/v solution of CHEMKLEEN 2010LP with 0.125% CHEMKLEEN 181ALP added. The panels were rinsed by immersing for approximately ten (10) seconds into deionized water, followed by an approximately ten (10) second spray with deionized water.
• a group of panels was then processed through the bath.
• the group consisted of the following: eight 4" x 12" hot dipped galvanized panels; two 4" x 6" hot dipped galvanized panels; one 4" x 6" panel of aluminum (6111 T43); and one 4" x 6" panel of cold rolled steel.
• the amount of surface area in this group was identical to the panel groups from Example 1 ; the ratio of zin-coated (galvanized) to cold rolled steel to aluminum was also the same, except that in this Example the galvanized metal consisted entirely of hot dipped galvanized panels.
• the panels were immersed into the pretreatment bath for two (2) minutes at approximately 73°F (23°C), with mild agitation. Next, the panels were rinsed with an approximately 10 - 15 second spray with deionized water, and dried with a warm air blow- off.
• each of the pretreatment baths was measured for zirconium level, pH, and fluoride level using the methods previously described.
• Example 2 Based on these measurements, the replenisher composition of Example 2 was added to the bath to adjust the zirconium level of the bath back to the starting value. Adjustments to bring the pH within the range of 4.5 - 4.8 and free fluoride level within the range of from 100-160 ppm were also made, if any adjustment was necessary. The pH was adjusted (if necessary) by adding CHEMFIL BUFFER to the bath. Free fluoride was adjusted (if necessary) by adding ZIRCOBOND CONTROL #4 to the bath.

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