US3364081A - Aqueous phosphating solutions - Google Patents

Aqueous phosphating solutions Download PDF

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US3364081A
US3364081A US425949A US42594965A US3364081A US 3364081 A US3364081 A US 3364081A US 425949 A US425949 A US 425949A US 42594965 A US42594965 A US 42594965A US 3364081 A US3364081 A US 3364081A
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solution
parts
metal
phosphating
phosphate
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John W Forsberg
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MAN-GILL CHEMICAL COMPANY AN OH CORP
Lubrizol Corp
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Lubrizol Corp
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Priority to US425949A priority Critical patent/US3364081A/en
Priority to GB51026/65A priority patent/GB1083474A/en
Priority to JP41000991A priority patent/JPS5113736B1/ja
Priority to DEL52596A priority patent/DE1285831B/de
Priority to FR45926A priority patent/FR1463618A/fr
Priority to US672672A priority patent/US3519783A/en
Priority to US672673A priority patent/US3502511A/en
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Assigned to MAN-GILL CHEMICAL COMPANY, AN OH CORP. reassignment MAN-GILL CHEMICAL COMPANY, AN OH CORP. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ROHCO, INC., AN OH CORP.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B23MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23KSOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
    • B23K35/00Rods, electrodes, materials, or media, for use in soldering, welding, or cutting
    • B23K35/22Rods, electrodes, materials, or media, for use in soldering, welding, or cutting characterised by the composition or nature of the material
    • B23K35/226Non-corrosive coatings; Primers applied before welding
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/10Orthophosphates containing oxidants
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    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D13/00Electrophoretic coating characterised by the process
    • C25D13/20Pretreatment
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/02Water
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/08Inorganic acids or salts thereof
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/08Inorganic acids or salts thereof
    • C10M2201/081Inorganic acids or salts thereof containing halogen
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/08Inorganic acids or salts thereof
    • C10M2201/082Inorganic acids or salts thereof containing nitrogen
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/08Inorganic acids or salts thereof
    • C10M2201/084Inorganic acids or salts thereof containing sulfur, selenium or tellurium
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/087Boron oxides, acids or salts
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/18Tall oil acids
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2211/00Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
    • C10M2211/08Halogenated waxes
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2215/042Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms containing hydroxy groups; Alkoxylated derivatives thereof
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/26Amines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2217/00Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2217/04Macromolecular compounds from nitrogen-containing monomers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2217/046Polyamines, i.e. macromoleculars obtained by condensation of more than eleven amine monomers
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2217/00Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2217/06Macromolecular compounds obtained by functionalisation op polymers with a nitrogen containing compound
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/02Groups 1 or 11
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    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10Semi-solids; greasy
    • CCHEMISTRY; METALLURGY
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    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2080/00Special pretreatment of the material to be lubricated, e.g. phosphatising or chromatising of a metal

Definitions

  • Aqueous solutions containing phosphate, nitrate and lead ions are useful for forming phosphate coatings on metal surfaces. Such coatings may be formed by contacting the metal with the solution at room temperature.
  • the phosphate solutions are particularly useful in that they improve the drawing properties of metals treated therewith, and metal surfaces thus treated remain weldable.
  • the phosphate coatings also improve the adhesion of siccative organic coatings to the metal.
  • This invention relates to novel aqueous phosphating solutions.
  • it relates to novel aqueous phosphating solutions containing lead ions; to the method of phosphating metal articles with these solutions; and to the metal articles which have been phosphated by these solutions.
  • metal surfaces such as aluminum, ferrous, and zinc surfaces may be provided with an inorganic phosphate coating by contacting them with an aqueous phosphating solution.
  • the phosphate coating protects the metal surface to a limited extent against corrosion and serves primarily as an excellent base for the later application of siccative organic coating compositions such as paint, lacquer, varnish, primers, synthetic resins, enamel, and the like.
  • Such inorganic phosphate coatings are generally formed on a metal surface by means of aqueous solutions which contain the phosphate ion and, optionally, certain auxiliary ions including metallic ions such as sodium, manganese, zinc, cadmium, copper, and antimony ions.
  • aqueous solutions may also contain non-metallic ions such as ammonium, chloride, bromide, fluoride, nitrate, sulfate, and borate ions.
  • These auxiliary ions influence the reaction with the metal surface, modify the character of the phosphate coating, and adapt it for a wide variety of applications.
  • an oxidizing agent such as sodium chlorate, potassium perborate, sodium nitrate, ammonium nitrate, sodium chlorite, potassium perchlorate, or hydrogen peroxide is included in the phosphating solution to depolarize the metal surface being treated and thereby increase the rate at which the phosphate coating is formed on the metal surface.
  • Other auxiliary agents such as anti-sludging agents, coloring agents, and metal cleaning agents may also be incorporated in the phosphating solution.
  • One common type of commercial phosphating solution which contains zinc ion, phosphate ion, and a depolarizing agent is made by dissolving small amounts of zinc dihydrogen phosphate, sodium nitrate, and phosphoric acid in water.
  • Such phosphating solutions, and others known in the metal finishing art, have been useful in providing an adherent, integral phosphate coating on metal articles, particularly ferrous metal articles and galvanized ferrous metal articles, thereby improving the adhesion thereto of a film of a subsequently applied siccative organic coating composition.
  • the use of the prior art phosphating process has been seriously curtailed in some applications for one or more of the following reasons: (1) the phosphating processes required that the phosphating solution be maintained at a temperature of at least about 150 F.; (2) metal surfaces which had been phosphated could not be welded satisfactorily; and (3) the electrodeposition of paint over phosphated metal articles required higher wattages than for plain steel.
  • Conventional commercial phosphate coatings appear to interfere with the passage of the welding current and result in poor welds and/or premature destruction of the electrodes by excessive arcing.
  • Any phosphating process adds to the cost of finishing a metal article and, in many instances, this added cost becomes prohibitive when a metal article must be formed and spot-Welded before it is phosphated.
  • the formed and spot-welded metal article may be of such dimensions and shape that it cannot be phosphated conveniently over its entire surface by ordinary commercial phosphating procedures.
  • the spot-welding of such phosphating steel has been unsuccessful for the reasons indicated above.
  • not all phosphate coatings are able to withstand the high pressures and temperatures required in the forming of the metal.
  • a definite need has existed for a phosphate coating which can be easily applied to metal surfaces and can be easily welded and formed.
  • Another object is to provide novel aqueous phosphating solutions which are adapted for phosphating metal articles.
  • Another object is to provide novel aqueous phosphating solutions which are adapted for phosphating ferrous, zinc, and aluminum surfaces.
  • Another object is to provide a method for forming an adherent phosphate coating on metal articles.
  • Another object is to provide metal surfaces which have been provided with an adherent phosphate coating.
  • Another object is to provide metal surfaces which have been provided with an adherent phosphate coating which is effective to inhibit the corrosion of the metal.
  • Another object is to provide metal surfaces which have been provided with an adherent phosphate coating which is effective to improve the drawing properties of the metals.
  • Another object is to provide metal surfaces which have been provided with an adherent phosphate coating which does not interfere with the weldability of the metal.
  • Still another object is to provide metal surfaces which have been provided With an adherent phosphate coating which is effective to improve the electrophoretic deposition of paint films on the metal surfaces.
  • Still another object is to provide metal surfaces which have been provided with an adherent phosphate coating which is eifective to improve the drawing properties of the metal and which coating does not diminish the weldability of the metal.
  • a further object is to provide metal surfaces which have been provided with an adherent phosphate coating which effectively prevents corrosion, improves the drawing properties of the metal, does not interfere with weldability of the metal and when free of drawing lubricants and other industrial soils serves as an excellent base for paints.
  • aqueous phosphating solution consisting essentially of phosphate ion, nitrate ion, and lead ion.
  • the aqueous phosphating solution will have a total acidity within the range of from about 5 to 850 points and will consist essentially of from about 0.10% to about 40% of phosphate ion, from about v.3 0.20% to about 55% of nitrate ion, and from about 0.20% to about 30% of lead ion.
  • a halide ion such as chloride, bromide, fluoride, and iodide ions is found to be beneficial in that it tends generally to provide a coating having fine crystals.
  • a halogen ion may be incorporated into the phosphating solution, generally in the form of their salts such as sodium fluoride, sodium chloride, sodium bromide, sodium iodide, potassium chloride, ammonium chloride, etc.
  • the aqueous phosphating solutions should generally have a total acidity within the range of from about 50 to about 400 points, a phosphate ion concentration of from about 0.5% to about 35%, a nitrate ion concentration of from about 2.0% to about 33%, and from about 1.0% to about 25% of lead ion.
  • aqueous phosphating solutions having a total acidity higher than 400 points, e.g., 700 points makes it possible to form satisfactory phosphate coatings on ferrous, zinc, and aluminum surfaces in as short a time as one second.
  • the commercial applications of such rapid phosphating processes are manifold.
  • points total acidity as employed in the phosphating art and this specification represents the number of milliliters of 0.1 normal sodium hydroxide solution required to neutralize a 10 milliliter sample of a phosphating solution in the presence of phenolphthalein as an indicator.
  • phosphating step may be accomplished.
  • any of the commonly used phosphating techniques such as spraying, brushing, dipping, roller-coating, and flow-coating can be employed.
  • the temperature of the aqueous phosphating solution may vary within wide limits, e.g., from about room temperature to about 240 F. In general, the best results are obtained when the aqueous phosphating solution is used at a temperature of from about room temperature to about 150 F.
  • a particular feature of the aqueous phosphating solutions of this invention is that a satisfactory phosphate coating can be deposited in a relatively short period of time at room temperature. If desired, however, the aqueous phosphating solution may be used at higher temperatures, e.g., 225 F., 250 F, or even 300 F., by employing superatmospheric pressures.
  • a surface is usually cleaned by a physical and/ or chemical means to remove any grease, dirt, or oxides.
  • the cleaned article is then ordinarily rinsed with water before being subjected to the phosphating treatment.
  • the phosphating operation is usually carried out until the weight of the phosphate coating formed on the metal surface is at least about 25 milligrams per square foot of surface area and is preferably within the range of from about 50 to about 1000 milligrams per square foot.
  • the time required to form the phosphate coating will vary according to the temperature, the concentration of the phosphate solution employed, the particular technique of applying the phosphating solution, and the coating weight desired.
  • the time required to produce a phosphate coating of a weight suitable for the purposes of this invention will be within the range of from about seconds to about 5 to minutes.
  • the immersion technique is preferred. This can be a simple dipping technique or a continuously moving kind of im- L'Il 4- mersion exemplified by the immersion of moving steel strip or zinc coated stock in the phosphating solution by means of submerged rollers or other devices Wh1ch serve the same purpose. Similarly, plates of heavy gauge steel may be conveyed continuously through the phosphating solution.
  • the temperature of the phosphating solution should be preferably between 200 F. for rapid phosphating action and the total immersion time being from about 1 to 20 seconds.
  • the phosphated metal article Upon completion of the phosphating operation, the phosphated metal article is generally rinsed with water and/or a hot dilute aqueous solution of chromic acid containing from about 0.01 to about 0.2% of CrO
  • the chromic acid rinse appears to seal the phosphate coating and improve its utility as a base for the application of the siccative organic coating.
  • Dilute aqueous solutions of metal chromates, metal dichromates, chromic acidphosphoric acid mixtures, and chromic acid-metal dichromate mixtures may also be used in place of the dilute aqueous chromic acid.
  • the phosphating solutions of this invention can be prepared by dissolving sufficient phosphoric acid, nitric acid, and lead oxide and an alkali metal halide (if desired) in water to yield the desired weight percentages of phosphate, nitrate, lead, and halide ions.
  • the points total acid may be adjusted by additional phosphoric and/or nitric acid.
  • salts, bases, and mineral acids such as ammonium dihydrogen phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate, potassium nitrate, sodium nitrate, ammonium nitrate, lead nitrate, ammonium chloride, sodium chloride, sodium bromide, sodium fluoride, and nickel nitrate, may be substituted inthe preparation of the phosphating solutions of this invention.
  • the ions of the phosphating solutions of this invention may be derived from a variety of compounds and it appears to be of little consequence whether or not these ions come from different salts or acids. Regardless of the identity 0 of the salts selected to provide the required ions, the
  • the phosphating solution may be prepared as a concentrate or as a dilute solution ready for use.
  • the presence of the lead ion in the aqueous phosphat ing solutions of this invention is essential if the novel properties of the phosphate coatings deposited by these aqueous phosphating solutions are to be obtained.
  • the nitrate ion serves as an oxidizing agent to depolarize the metal surface and increase the coating speed of the phosphating solution.
  • the incorporation of halogen ions such as the fluoride and chloride ions is not essential but appears to improve the crystallinity and uniformity of the deposited coating.
  • the coating action of the phosphating solutions certain surface-active agents. These agents also serve as dispersants in the phosphating solution and help to maintain the ingredients in solution. Examples of such agents which have been found to be particularly effective are the ethylene oxide condensates, particularly those containing from about 3 to about 25 polyoxyethylene groups such as polyoxyethylene derivatives of oleic acid and polyoxyethylene alkyl phenol derivatives. Also useful as surface-active agents in the coating compositions of this invention are sodium alkyl sulfates, and sulfonated hydrocarbons such as alkyl naphthalene sulfonic acid. It will be appreciated that the surface-active agent selected must be compatible with the acidic phosphate solutions of this invention. Another important requirement of the surface-active agent is that the agent, when added to the phosphating solution, should improve the performance of the solution without afiectingor inhibiting the essential ingredients of the aqueous phosphating solutions of this invention.
  • the nature of the coating compositions deposited by the aqueous phosphating solutions of this invention is not known with certainty but preliminary investigation (X-ray analysis) indicates that the coating is primarily a lead phosphate of apatite structure (Ph (OH) (PO When a halogen such as chlorine is incorporated into the phosphating solution, the structure of the coating composition appears to be mostly Pb (Cl (PO or a mixture of these two lead phosphates.
  • a concentrate is prepared by adding 204 parts of commercial 70% nitric acid, 54.4 parts of potassium nitrate, and 53.3 parts of commercial 85% phosphoric acid to 540 parts of water. The mixture is stirred and 86 parts of lead oxide is added followed by the addition of 2 parts of sodium chloride.
  • a working solution having a total acidity of 160 points is prepared by adding 223 parts of the above concentrate to 239 parts of water.
  • a phosphating solution having a total acidity of 9 points is prepared by dissolving 230 parts of the concentrate prepared for Solution B in 7,437 parts of water.
  • a phosphating solution having a total acidity of 36.5 points is prepared by dissolving 230 parts of the concentrate of Solution B in 1,680 parts of water.
  • a phosphating solution having a total acidity of 76.5 points is prepared by dissolving 230 parts of the concentrate of Solution B in 727 parts of water.
  • the phosphate solution having a total. acidity of 254 points is prepared by adding 230 parts of the concentrate of Solution B to 84 parts of water.
  • a phosphating solution having a total acidity of 608 points is prepared by dissolving 230 parts of the concentrate of Solution B in 84 parts of water and 70 parts of commercial 85 phosphoric acid.
  • SOLUTION K A concentrate is prepared by adding 2,040 parts of commercial 70% nitric acid, 544 parts of potassium nitrate, and 533 parts of commercial 85% phosphoric acid to 5,400 parts of water. The mixture is stirred and 860 parts of lead oxide is added slowly. Stirring is continued until all of the lead oxide is in solution. Two parts of the wetting agent of Solution A solution having a total acidity of 159 points is prepared by dissolving 223 parts of the above concentrate in 239 parts of water.
  • a phosphating P7 4 SOLUTION N To 936 parts of water there is added 108 parts of commercial 70% nitric acid, 20 parts of lead oxide, 12 parts of arrmoniurn dihydrogen phosphate and 0.4 part of sodium chloride.
  • a concentrate is prepared from 1,315 parts of commercial 70% nitric acid, 148 parts of commercial 85% phosphoric acid, 360 parts of potassium nitrate, 482 parts of lead oxide, 9 parts of sodium chloride and 2 parts of the wetting agent of Solution A.
  • the solution is prepared by dissolving 4,995 parts of the above concentrate in 7,605 parts of Water.
  • One feature of the combination of ions which characterizes the phosphating solutions of this invention is that such solutions may be utilized to deposit uniform coatings on ferrous metal articles, galvanized ferrous metal articles, aluminum articles, and mixtures of ferrous and galvanized ferrous metal articles.
  • a particular feature of the phosphating solution of this invention is the unique properties of the coatings which are deposited by these solutions on metal articles. For example, metal surfaces which have been coated in accordance with the process of this invention remain weldable. Furthermore, the coating deposited by the solutions of this invention improves the drawing properties of the metals thus coated, and facilitates cold drawing in manufacturing operations.
  • the smooth, uniform coating also provides for protection against corrosion, and is an excellent base for siccative organic coating compositions.
  • the amounts of the various ions in the aqueous phosphating solutions of this invention may be varied depending upon the type of metal article being treated and the particular technique being employed.
  • the phosphate ion, nitrate ion, and lead ion concentration may be as high as 40%, 55% and 30% respectively. More dilute concentrations are preferred where rapid phosphating is not essential.
  • metal articles are easily phosphated by immersion for a period of from seconds to 1 to 2 minutes in a phosphating solution having a total acidity of about 50 to about 400 points.
  • Example 1 The ability of the phosphate coatings deposited by the solutions of this invention to resist corrosion is shown by the results of the following outdoor humidity test.
  • 4 X 8" 20-gauge SAE 1020 cold-rolled, phosphated steel panels (no top coat) were placed in a hori zontal position approximately two feet above a pan of water in an enclosed outdoor shed. After being exposed in this manner for seven weeks, the panels were removed and inspected for rust.
  • Table II The results of this outdoor humidity test, as shown in Table II, indicate that the phosphate coatings deposited by the aqueous phosphating solutions of this invention are effective to reduce the corrosion of steel surfaces.
  • Example 2 After a metal article has been phosphated in accordance with the present invention, it is often desirable to apply a decorative and protective top-coat of a siccative organic coating composition such as paint, lacquer, varnish, synthetic resins, enamel, and the like.
  • a siccative organic coating composition such as paint, lacquer, varnish, synthetic resins, enamel, and the like.
  • synthetic resins which may be used are the acrylic, alkyd, epoxy, phenolic, and polyvinyl alcohol resins.
  • Coating composition A White alkyd baking primer
  • Percent Short soya alkyd (50% solution in xylene of Titanium dioxide l8 Barium sulfate 12
  • Magnesium silicate 10 Short soya alkyd (50% solution in xylene of alkyd resin prepared from 41.6 parts of phthalic anhydride, 18.4 parts of glycerol and parts soya bean acid)
  • Xylene 14.8 Cobalt naphthenate (6% Co) 0.1
  • Coating composition B red oxide resin modified alkyd baking primer
  • Red iron oxide 85% F20,3
  • Magnesium silicate 8.2 Resin modified alkyd (70% xylene) 28.6 Naphtha 6.6 Xylene 21.8 Mineral spirits 5.5 Cobalt naphthenate (6% Co) 0.2
  • Coating composition C (white alkyd baking topcoat):
  • Titanium dioxide 29.2 Medium castor alkyd solution in xylene of an alkyd resin prepared from 38 parts of phthalic anhydride, 14 parts of glycerol, and 48 parts of castor oil) 48.6 Mineral spirits 19.9 Xylene 2.2 Cobalt naphthenate (6% Co) 0.1 Coating composition D (White acrylic baking topcoat):
  • Titanium dioxide 25.0 Thermosetting acrylic resin (50% in xylene) 60.0 Xylene 12.2 Cellosolve acetate 2.7 Anti-skinning agent 0.1 Coating composition E (white alkyd baking topcoat):
  • Titanium dioxide 28.4 Medium cottonseed alkyd resin (a solution of an alkyd prepared from 40 parts of phthalic anhydride, 25 parts of glycerol, and 35 parts of cottonseed oil in xylene) 48.8 High flash naphtha 1.5
  • Coating composition F White vinyl baking topcoat
  • Titanium dioxide 20.0 Resin stabilizer 0.7 Vinyl chloride-vinyl acetate copolymer 15) w. 12.5 Toluene 29.5 Methyl isobutyl ketone 29.5 Epichlorohydrin 0.1 Methanol 0.1 Tricresyl phosphate 7.2
  • Coating composition G (white modified alkyd baking topcoat): Percent Titanium dioxide 26.8 Zinc oxide 1.4
  • Coating composition H red lead alkyd air dry primer
  • the organic coating compositions can be effected by any of the ordinary techniques such as brushing, spraying, dipping, roller-coating, flow-coating, etc.
  • the topcoated phosphated article is dried in the manner best suited for the particular siccative organic coating composition employed such as air-drying at ambient temperature, drying in a current of hot air, baking in an oven, or baking under a battery of infra-red lamps.
  • the thickness of the dried film of the siccative organic coating composition will be within the range of from about 0.1 to about 10 mils, more often from about 0.3 to about 5 mils.
  • the scored panels were then subjected to the salt-fog test described in ASTM Procedure B11762.
  • the panels are placed in a cabinet containing a 5% aqueous sodium chloride solution at 95 F. Air is bubbled through the solution to produce a corrosive salt atmosphere which acts on the surface of the test panels, suspended above the level of the salt solution.
  • the panels are allowed to remain in this atmosphere for 168 hours whereupon they are removed, washed with water, and dried with a cloth. A pressure sensitive tape is then applied to the panel and removed suddenly. This procedure is repeated until no more paint can be removed in this manner. The panels are then inspected to determine the amount (percent) of paint still adhering to the metal substrate. The loss of adhesion caused by corrosion from the scribed lines is measured in thirty-seconds of an inch. This corrosion along the scribed lines is called creep.
  • Example 3 As mentioned previously, the coatings deposited by the aqueous phosphating solutions of this invention are particularly useful in the preparation of metals for drawing and forming operations. Before a metal is subjected to a drawing operation, it is generally covered with a lubricant. Metal drawing lubricants are generally classified into two groups commonly referred to as wet lubricants and dry lubricants. Both types are applied as liquids, the wet lubricant remaining liquid, but the dry lubricant being dried to form a solid film. The wet lubricants are more easily applied and require a minimum amount of floor space and equipment. These lubricants are usually applied 'by spraying, swabbing, or with a roller. Spraying is generally unsatisfactory because of the waste due to over-spraying.
  • lubricants which have been found useful as aids in the drawings of metal include petroleum oils, e.g., 5,000 'S.S.U. at F.; chlorinated wax; soaps prepared by neutralizing mixed fatty acids with a mixture of amines and caustic soda; dispersions of such soaps; beeswax; dry soap type films; heavy or light duty pigmented emulsions; heavy duty non-pigmented emulsions; etc.
  • the following lubricants are examples of coating compositions which will produce films which have satisfactory drawing properties.
  • Drawing lubricant G Sodium stearate 45 Sodium sulfite 4 Borax 38 Water 5 Drawing lubricant H
  • Chlorinated wax (50% chlorine) SAE mineral lubrication oil The solid lubricants such as those illustrated by lubricants E and F may be applied to the metal surface in paste form by adding a small amount of water, or the metal surface may be coated by immersion in a boiling solution containing about 1 pound of the lubricant per gallon of water.
  • the lubricant which is chosen for this purpose must have the ability to allow the metal to flow properly and to minimize ga'lling and scoring of the tools and/or the fabricated parts.
  • an important feature of any lubricant system is the ability of the lubricant to reduce or control friction.
  • a lubricated test strip (2" x 24") is placed between a pair of flat polished dies upon which is placed a load by means of a calibrated torque wrench acting on a screw.
  • the dies may be heated to increase the severity of the test condition.
  • This assembly is mounted in a tensile testing machine and the metal strip is moved through the dies. The force (measured in pounds) required to move the strip at a rate of 4 inches per minute through the dies at a given temperature and jaw load is observed and recorded.
  • the results of the test are reported in terms of dynamic coefficient of friction which is defined by the following equation:
  • Example 4 Immersion Soln temp. Coating wt. Friction b Time (sec) F.) (mg/ft?) A commercial drawing lubricant is applied over the panels before Example 4 Metal articles which have been phosphated in accordance with the process of this invention are easily Welded. This property is especially significant because inorganic phosphate coatings on metal surfaces generally prevent welding or cause the welding of such treated metal articles to be extremely diffioult.
  • the welding operation may be carried out by the use of procedures and equipment commonly employed for the purpose. No special precautions are necessary and adjustments with respect to welding current, welding time and electrode pressure may be made in the manner known to those versed in the art of welding.
  • Wnrmrxc TEST A large number of clean, degreased, 4 x 12" panels of SAE 1020 ZO-gauge cold-rolled steel were phosphated by immersion in solution F for 20 seconds at a temperature of about 130 F. Thereafter, the panels were water-rinsed, and immersed for 10 seconds in an aqueous solution of chromic acid at room temperature and blown dry with warm air. The phosphate coating weight on the panels was found to be 300: mg. per square foot.
  • test is terminated if there is constant or violent metal expulsion, or excessive smoke or fumes which are irritating to the operator.
  • the button diameter was observed to be substantially the same as the first button, and the electrodes were still in good condition and did not require dressing.
  • Example 3 The durability and versatility of the phosphate coatings deposited by the solutions of this invention are shown by the following procedure which compares the corrosion resistance of phosphated and non-phosphated steel panels before and after being subjected to the sliding friction test of Example 3.
  • the cleaned, welded panels were then spray-painted with a one-coat white, amine modified alkyd-based appliance paint which was then baked for 30 minutes at 300 F.
  • the average combined coating thickness was approximately 1 mil.
  • the paint film on each panel was ruptured by scoring a 6-inch line to the bare metal of each panel, and the panels were subjected to the salt-fog test described in Example 2 for a period of 72 hours. After being exposed to the salt fog, the panels were removed, washed with water, and dried with a cloth.
  • the amount of paint still adhering to the metal substrate was determined according to the procedure described in Example 2.
  • Table V indicate that the coatings deposited by the aqueous phosphating solutions of this invention maintain their corrosion resisting properties even after the drawing operation.
  • the metal article to be coated is placed in an electrolytic solution which contains emulsified colloidal paint particles,
  • An electric charge is routed through both the metal surface and the water-based primer by placing a positive charge on the metal surface (acting as an electrode) and a negative charge on a second electrode, generally the container.
  • the colloidal particles of the primer which are in suspension move either toward the negative or positive electrode depending on the charge carried by the dispersed particles.
  • negative paint particles are attracted to the metal surface.
  • the colloidal particles lose their electrical charge, thereby breaking the emulsion and depositing as a coating on the electrode.
  • the metal article is then removed from the solution, rinsed, and baked in an oven to cure the electrophoretically deposited coating.
  • the electrical potential applied in the process of electrophoresis will be determined by the thickness of the desired coating, the conductivity and composition of the coating bath, and the time allotted for the formation of the coating. Voltages of from 50 to about 1000 volts have proven satisfactory at a current density of from 0.1 to about 5 amperes per square foot.
  • the electrolytic solutions which are utilized in the electrophoretic coating processes generally comprise emulsified paint particles in a colloidal state dispersed in a conducting liquid medium.
  • a red primer which may be electrophoretically deposited is prepared as follows. A mixture of 63 parts (all parts are by weight unless otherwise specified) of a film-forming material consisting of a styrene-allyl alcohol copolymer is mixed with 37 parts of linseed fatty acid, and the mixture is esterified at 260 C. to an acid number of 5 and a maximum viscosity of about 2.5 poises measured when the copolymer is reduced to a 60% solution in xylene.
  • Ffty-one parts of the above prepared mixture is blended in a roller mill with 45 parts of red oxide pigment and 4 parts of linseed fatty acids. This blended mixture (38 parts) is further blended with 50 parts of the above film forming mixture, 11.8 parts of melamine formaldehyde, and 0.2 part of cobalt naphthenate.
  • An emulsifying agent is prepared consisting of 3.5 parts of commercial 28% ammonium hydroxide and 96.5 parts of demineralized water. The emulsifying agent is added slowly to the paint mixture until the so-called inversion point is reached. The balance of the diluted ammonium hydroxide is then added, and the resulting emulsion is further refined in a colloid mill to produce a more stable emulsion.
  • the above described paint composition is useful as an automobile primer paint and may be electrophoretically deposited on automobile parts from an electrolyte prepared by mixing 2 parts of the above paint composition with 6 parts of water and A: part of concentrated ammonia.
  • the resulting electrolyte is a colloidal dispersion.
  • the metal surface is generally pretreated with, for example, a phosphate solution.
  • a phosphate solution Ordinarily the phosphate coatings deposited by the known phosphating solutions such as those which deposit zinc phosphate, manganese phosphate, one or more alkaline earth metal phosphates, or zinc or manganese phosphate modified with an alkaline earth metal phosphate, increase the electrical resistance of the metal surface. In such cases, greater poW-' er (wattage) is required to electrophoretically deposit a satisfactory coating of paint on the metal surface.
  • metal surfaces which are coated with the phosphate coatings of this invention can be electrophoretically coat- I 5 ed with paint at a power input which is less than that required for plain steel. This unusual effect is demonstrated as follows.
  • an aqueous paint solution is prepared by dissolving one part of a commercial water-soluble red oxide primer in 3 parts of distilled water, placed in a stainless steel container, and maintained at a temperature of about 73 76 F.
  • a magnetic stirrer is used to keep the solution circulating.
  • a 5 ampere power supply (0 to 500 volts DC output) is used to supply the current.
  • the steel panels (4" X 8" 20 gauge strip steel) are pretreated and electrocoated one at a time by applying a positive charge on the test panel and a negative charge on the steel container.
  • the power supply is adjusted to give 1.1 amperes constant current in 25 seconds, and this current is maintained at this level while the voltage is increased to a level which will result in 45 seconds, in a deposition of a cured coating of about 1 mil thickness. This voltage is recorded as the constant peak voltage.
  • the power is turned oft and the coated panel is removed from the electrolyte, rinsed with cold water, and baked in an oven at 350 2 10 F. for 20 minutes.
  • Example 7 The utility of the coating compositions obtained by the process of this invention as paint bases is further illustrated by subjecting the electrophoretically painted, phosphate coated steel panels to the salt fog corrosion test described in Example 2 with the following changes: The test is run for 240 hours; and no tape is applied to the tested panels before they are rated. The results of this salt fog corrosion test, as shown in Table VII, indicate that the aqueous phosphating solutions of this invention substantially improve the rust preventive properties of painted' steel panels. This is demonstrated by the improved resistance to undercutting by corrosion from the scribed TABLE VIII.SALT
  • Table VIII contains a comparison of the salt-fog test results on the above described test shapes using (1) plain steel, (2) plain steel which was formed and welded before a zinc phosphate coating was deposited, and (3) steel panels which were phosphated according to the process of this invention before the panels were formed and welded into the test shape.
  • the procedure for preparing the zinc phosphate test shapes of (2) differs from the procedure in (3) because the zinc phosphate coated steel panels cannot be welded together, thus, the welding step must be carried out before the panels are phosphated with this solution.
  • Example 9 The ease with which panels, coated in accordance with the process of this invention, can be welded and electrocoated is believed to be a result of the electrical conducivity of the novel phosphate coatings, another unique property.
  • the use of the wellknown aqueous phosphating solutions such as those depositing a zinc phosphate type of coating may not be satisfactorily welded, and attempts to electrocoat such coated panels require added power input.
  • the following test was devised.
  • An aqueous phosphating solution having a total acidity within the range of from about 5 to 850 points and consisting essentially of from about 0.10% to about 40% of phosphate ion, from about 0.20% to about 55% of nitrate ion, and from about 0.20% to about 30% of lead ion.
  • An aqueous phosphating solution having a total acidity within the range of from about 50 to about 400 points and consisting essentially of from about 0.5% to about 35% of phosphate ion, from about 2.0% to about 33% of nitrate ion, and from about 1.0% to about 25% of lead ion.
  • An aqueous phosphating solution having a total 18 acidity within the range of from about to about 300 points and consisting essentially of from about 0.5 to about 30% of phosphate ion, from about 2.0% to about 25 of nitrate ion and from about 1.0% to about 20% of lead ion.
  • An aqueous phosphating solution having a total acidity within the range of from about 100 to about 300 points and consisting essentially of from about 0.5 to about 30% of phosphate ion, from about 2.0% to about 25% of nitrate ion, from about 1.0% to about 20% of lead ion and from about 0.002% to about 0.5 of chloride ion.
  • a method for forming an adherent phosphate coating on metal articles which comprises contacting said articles with the aqueous phosphating solution of claim 1 at a temperature of at least about 50 F.
  • a method for forming an adherent phosphate coating on metal articles which comprises contacting said articles with the aqueous phosphating solution of claim 2 at a temperature within the range of from about 50 F. to about 200 F.
  • a metal article which has been provided with an adherent phosphate coating in accordance with the meth- 0d of claim 7.
  • a method for improving the adhesion of a siccative organic coating composition to metal articles which comprises contacting said articles, prior to the application of said organic coating compositions, with the aqueous phosphating solution of claim 1 at a temperature of at least about 50 F.
  • a process for treating metal surfaces to facilitate the cold drawing thereof comprising the steps of (1) contacting said metal article with the aqueous phosphating solution of claim 1 at a temperature of at least about 50 F. to provide a phosphate coating thereon, and (2) contacting said phosphate-coated metal surface with a drawing lubricant.

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GB51026/65A GB1083474A (en) 1965-01-15 1965-12-01 Aqueous phosphating solutions
JP41000991A JPS5113736B1 (zh) 1965-01-15 1966-01-10
FR45926A FR1463618A (fr) 1965-01-15 1966-01-14 Solutions aqueuses de phosphatation
DEL52596A DE1285831B (de) 1965-01-15 1966-01-14 Phosphatierungsloesung
US672672A US3519783A (en) 1965-01-15 1967-08-30 Welding process
US672673A US3502511A (en) 1965-01-15 1967-08-30 Electrophoretic coating process

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US3454483A (en) * 1964-04-30 1969-07-08 Hooker Chemical Corp Electrodeposition process with pretreatment in zinc phosphate solution containing fluoride
US3516875A (en) * 1966-06-11 1970-06-23 Hooker Chemical Corp Process for coating ferrous surfaces
US3518129A (en) * 1968-01-11 1970-06-30 Lubrizol Corp Novel phosphating solutions containing lead and fluoride ions
JPS4958033A (zh) * 1972-10-09 1974-06-05
US4114505A (en) * 1977-01-31 1978-09-19 Loeser William J Coatings and methods of application
US4639295A (en) * 1984-08-14 1987-01-27 Amchem Products, Inc. Zinc phosphating method
US4788086A (en) * 1984-07-14 1988-11-29 Nippondenso Co., Ltd. Copper-based metallic member having a chemical conversion film and method for producing same
US20050208224A1 (en) * 2002-03-20 2005-09-22 Goran Stenberg Method for applying an anti-corrosion coating to especially corrosion exposed parts in rock drill equipment
WO2010046243A1 (de) * 2008-10-20 2010-04-29 Basf Se Kontinuierliches verfahren zur oberflächenbehandlung von metallbändern
CN101994107A (zh) * 2009-08-18 2011-03-30 邵阳市创捷化工有限公司 防腐膜及其生产工艺

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DE2736874A1 (de) * 1977-08-16 1979-03-01 Metallgesellschaft Ag Verfahren zur erleichterung der kaltumformung von metallen
EP0451437B1 (en) * 1990-04-09 1995-04-05 Kawasaki Steel Corporation A galvanized steel sheet with high press formability and a method for manufacturing the same
CN105728985A (zh) * 2016-05-04 2016-07-06 惠州市联镒铜线有限公司 一种助焊剂
CN112410772B (zh) * 2020-11-04 2023-01-20 安徽瑞荣汽车零部件有限公司 一种钢背的抛光磷化处理方法

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US2516008A (en) * 1948-06-19 1950-07-18 Westinghouse Electric Corp Composition and process for treating metal surfaces
US2813813A (en) * 1952-12-17 1957-11-19 Parker Rust Proof Co Process for forming protective phosphate coatings on metallic surfaces
US2890944A (en) * 1956-05-25 1959-06-16 North American Aviation Inc Continuous chemical milling process
US2921865A (en) * 1958-04-02 1960-01-19 Aluminum Res Corp Method of forming cold extrusion lubricants having a zinc phosphate undercoating
US3144360A (en) * 1962-02-19 1964-08-11 Lubrizol Corp Phosphating process
US3166444A (en) * 1962-04-26 1965-01-19 Lubrizol Corp Method for cleaning metal articles

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BE483275A (fr) * 1948-06-19 1948-07-15 Walterisation Company Ltd Procédé et bain pour la formation de revêtements protecteurs anticorrosion sur les surfaces métalliques

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US2516008A (en) * 1948-06-19 1950-07-18 Westinghouse Electric Corp Composition and process for treating metal surfaces
US2813813A (en) * 1952-12-17 1957-11-19 Parker Rust Proof Co Process for forming protective phosphate coatings on metallic surfaces
US2890944A (en) * 1956-05-25 1959-06-16 North American Aviation Inc Continuous chemical milling process
US2921865A (en) * 1958-04-02 1960-01-19 Aluminum Res Corp Method of forming cold extrusion lubricants having a zinc phosphate undercoating
US3144360A (en) * 1962-02-19 1964-08-11 Lubrizol Corp Phosphating process
US3166444A (en) * 1962-04-26 1965-01-19 Lubrizol Corp Method for cleaning metal articles

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3454483A (en) * 1964-04-30 1969-07-08 Hooker Chemical Corp Electrodeposition process with pretreatment in zinc phosphate solution containing fluoride
US3516875A (en) * 1966-06-11 1970-06-23 Hooker Chemical Corp Process for coating ferrous surfaces
US3518129A (en) * 1968-01-11 1970-06-30 Lubrizol Corp Novel phosphating solutions containing lead and fluoride ions
JPS4958033A (zh) * 1972-10-09 1974-06-05
US4114505A (en) * 1977-01-31 1978-09-19 Loeser William J Coatings and methods of application
US4788086A (en) * 1984-07-14 1988-11-29 Nippondenso Co., Ltd. Copper-based metallic member having a chemical conversion film and method for producing same
US4639295A (en) * 1984-08-14 1987-01-27 Amchem Products, Inc. Zinc phosphating method
US20050208224A1 (en) * 2002-03-20 2005-09-22 Goran Stenberg Method for applying an anti-corrosion coating to especially corrosion exposed parts in rock drill equipment
WO2010046243A1 (de) * 2008-10-20 2010-04-29 Basf Se Kontinuierliches verfahren zur oberflächenbehandlung von metallbändern
US20110017352A1 (en) * 2008-10-20 2011-01-27 Basf Se Continuous method for treating the surface of metal strips
KR101211307B1 (ko) 2008-10-20 2012-12-11 바스프 에스이 금속 스트립의 표면을 처리하는 연속 방법
US8372216B2 (en) 2008-10-20 2013-02-12 Basf Se Continuous method for treating the surface of metal strips
CN101994107A (zh) * 2009-08-18 2011-03-30 邵阳市创捷化工有限公司 防腐膜及其生产工艺
CN101994107B (zh) * 2009-08-18 2013-10-30 邵阳市创捷化工有限公司 防腐膜及其生产工艺

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FR1463618A (fr) 1966-12-23

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