US3597283A - Phosphating solutions for use on ferrous metal and zinc surfaces - Google Patents

Phosphating solutions for use on ferrous metal and zinc surfaces Download PDF

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US3597283A
US3597283A US864875A US3597283DA US3597283A US 3597283 A US3597283 A US 3597283A US 864875 A US864875 A US 864875A US 3597283D A US3597283D A US 3597283DA US 3597283 A US3597283 A US 3597283A
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per liter
ion
solution
zinc
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Charles T Snee
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MAN-GILL CHEMICAL COMPANY AN OH CORP
Lubrizol Corp
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Lubrizol Corp
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • 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
    • C23C22/12Orthophosphates containing zinc cations
    • C23C22/13Orthophosphates containing zinc cations containing also nitrate or nitrite anions
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36Chemical 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 containing also phosphates
    • C23C22/368Chemical 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 containing also phosphates containing magnesium cations
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12493Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/12535Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.] with additional, spatially distinct nonmetal component
    • Y10T428/12583Component contains compound of adjacent metal

Definitions

  • This invention relates to the treatment of metal surfaces, and more particularly to phosphating solutions used for such treatment. Still more particularly, it relates to an aqueous solution, suitable for producing a microcrystalline coating on both zinc and ferrous metal surfaces, containing as essential coating producing ingredients the following ions in the indicated concentrations:
  • A Phosphate3-2O grams per liter
  • B Zinc-0.5-3.0 grams per liter
  • C Nickel, cobalt or copper0.05-3.0, 0.003-0.7 or
  • Phosphate coatings are advantageously formed on both ferrous metal (e.g., cold-rolled steel) and zinc (e.g.,
  • a principal object of the present invention is to provide new phosphating solutions of improved versatilityv
  • a further object is to provide a phosphating solution which can be used on both steel and zinc surfaces without the necessity for changing, modifying or recharging the solution with a change in the metal being treated.
  • Still another object is to provide a phosphating solution which deposits a microcrystalline phosphate coating of improved crystal structure which adheres tightly to the metal surface being treated, serves as an excellent paint base and protects the surface from corrosion.
  • the phosphating solutions of this invention have six essential ingredients of which the first is, of course, the phosphate ion (Component A).
  • This may be provided by phosphoric acid, which is usually the most convenient source.
  • the commercially available phosphoric acid is usually employed, although condensed acids such as pyrophosphoric, polyphosphoric and the like are also suitable as are salts such as ammonium dihydrogen phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate and the like.
  • the phosphate ion concentration is about 3-20 grams per liter and is usually about 3-15 grams per liter, at least in fresh solutions.
  • Zinc ion may be provided by zinc oxide or by other water-soluble salts such as zinc nitrate, zinc fiuosilicate and the like.
  • the zinc ion concentration is about 0.5-3.0 grams per liter.
  • Nickel, cobalt and copper are considered equivalents as component C from the standpoint of function in the compositions of this invention. They vary, however, in the amounts used. Thus, the amount of nickel should be about ODS-3.0 grams per liter and preferably about 0.1-3.0 grams per liter. Cobalt is used in smaller amounts (about 0.003-0.7 gram per liter) and copper in still smaller amounts (about 0.003-0.04 gram per liter). These metal ions may be furnished by any of the ordinarily used soluble salts thereof, typically the nitrate. Of the three metals, nickel is preferred. 1
  • magnesium component D
  • component D is essential to the compositions of this invention, and may be furnished by magnesium oxide, magnesium nitrate, magnesium chloride or the like.
  • the magnesium concentration is 1-8 grams per liter, preferably about 2.5-6.0 grams per liter.
  • the accelerator used in the solutions of this invention is the nitrite ion (component B) which may be present in very small amounts, generally about 0.01-0.25 gram per liter. It is most conveniently provided as sodium nitrite, but other soluble nitrites such as magnesium, potassium or the like may be used.
  • Component F is one or both of fluoride and chloride ions.
  • the amount of fluoride should be about 0.1-3.0 grams per liter and preferably about 0.1-1.0 gram per liter.
  • the required amount of chloride ion is 2-30 grams per liter, preferably about 7-15 grams per liter. It may occasionally be convenient to use both ions, in which case the concentration of each may be in the indicated ranges and usually on the loW side thereof.
  • Typical sources of fluoride and chloride ions are the sodium, potassium, magnesium or ammonium salts thereof, or other equivalent salts.
  • Fluoride ion may also be provided in the form of a complex fluoride such as fluosilicate or fluoborate.
  • compositions of this invention may also contain other ions which, while not essential to their function, come into the solution because of their presence in salts which it is convenient to use to provide the essential ions.
  • nitrates of zinc, nickel and the like and therefore nitrate ion may be present in concentrations up to about 40 grams per liter.
  • Nitrate serves, or course, as an accelerator or depolarizer similar to nitrite, but its presence is not necessary since the nitrite ion provides all the depolarizing effect required.
  • the phosphating solution is generally adjusted, before use, to a total acidity of about -30 points and a very low free acidity; usually about 0.1-5.0 points.
  • the term points represents the number of milliliters of 0.1 N sodium hydroxide solution required to neutralize a 10 m1. sample of the phosphating solution.
  • the indicator used to determine total acid is phenolphthalein; for free acid, it is modified methyl orange.
  • the phosphating solution may be prepared in the form of one or more concentrates, or as a dilute solution ready for use.
  • nitrite ion When provided as a concentrate, nitrite ion must be excluded and added to the prepared solution just before use, since the highly acidic concentrate would convert nitrite to unstable nitrous acid.
  • the coating action of the phosphating solutions of this invention can be improved by the addition of surface-active agents.
  • These agents also serve as dispersants in the phosphating solution and help to maintain the ingredients in solution.
  • suitable surface-active agents are the ethylene oxide condensates, particularly those containing about 3-25 polyoxyethylene groups, of which typical examples are polyoxyethylene derivatives of oleic acid and of alkyl phenols.
  • sodium 'alkyl sulfates and sulfonated hydrocarbons such as alkylnaphthalenesulfonic acid.
  • EXAMPLE 1 A concentrate is prepared from 45.9 parts of 85% phosphoric acid, 8.2 parts of 67% nitric acid, 1.2 parts of magnesium oxide, 8.7 parts of zinc oxide, 6.0 parts of nickel nitrate hexahydrate, 1.9 parts of zinc fluosilicate hexahydrate, and 28.1 parts of water. This solution is diluted With water to a concentration of 1.33%. To this solution is added a mixture of 29.7 parts of 67% nitric acid, 7.3 parts of magnesium oxide, 20.0 parts of sodium nitrite and 43.0 parts of water, in an amount suflicient to increase the magnesium ion concentration to 3.0 grams per liter.
  • EXAMPLE 2 A concentrate is prepared containing 35.4 parts of 75% phosphoric acid, 8.3 parts of 67% nitroic acid, 14.0 parts of zinc oxide, 8.4 parts of nickel nitrate hexahydrate, 6.9 parts of zinc fluosilicate hexahydrate, and 33.5 parts of water. A second solution is prepared containing 11.0 parts of magnesium oxide, 44.8 parts of 67% nitric acid, and 44.2 parts of water. These solutions are combined and diluted to give a working solution With a phosphate ion concentration of 4.56 grams per liter and a magnesium ion concentration of 3.32 grams per liter. Aqueous sodium nitrite solution (28%) is added in an amount suflicient to provide 0.06 gram per liter of nitrite ion.
  • EXAMPLE 3 The phosphoric acid-containing concentrate of Example 2 is combined with a solution containing 12.5% magnesium oxide, 63.0% of 20% muriatic acid and 24.5% Water, and with the solution of sodium nitrite, in amounts suitable to provide 5.7 grams per liter of phosphate ion, 3.0 grams per liter of magnesium ion and 0.1 gram per liter of nitrite ion.
  • EXAMPLE 4 A solution is prepared containing 6.2 parts of phosphoric acid, 8.3 parts of 67% nitric acid, 14.0 parts of zinc oxide, 3.5 parts of nickel nitrate hexahydrate, and 14.0 parts of Water. A second solution is prepared containing 1015 parts of 67% nitric acid, 250 parts of magnesium oxide and 1000 parts of water. These solutions, and a 28% aqueous solution of sodium nitrite, are combined in proportions sufficient to provide 11.4 grams per liter of phosphate, 3.49 grams per liter of magnesium and 0.1 gram per liter of nitrite. Hydro fluoric acid is added in an amount suflicient to provide 0.3 gram per liter of fluoride ion.
  • EXAMPLE 5 A solution containing phosphoric acid, zinc oxide and nickel nitrate is prepared and combined with the magnesiumand nitric acid-containing solution of Example 4, the sodium nitrite solution of Examples 2-4 and hydrofluoric acid in amounts sufficient to provide 9.88 grams per liter of phosphate ion, 3.74 grams per liter of magnesium ion, 0.1 gram per liter of nitrite ion and 0.04 gram per liter of fluoride ion.
  • EXAMPLE 6 The procedure of Example 5 is repeated except that the magnesiumand nitric acid-containing solution is replaced by a magnesium chloride solution. The amounts used are sufficient to provide 9.5 grams per liter of phosphate ion, 4.1 grams per liter of magnesium ion, 0.1 gram per liter of nitrite ion and 10.8 grams per liter of chloride ion.
  • EXAMPLE 7 The procedure of Example 6 is repeated, except that hydrofluoric acid is added and the quantities of the various solutions are suflicient to provide 7.6 grams per liter of phosphate ion, 3.4 grams per liter of magnesium ion, 0.1 gram per liter of nitrite ion, 0.52 gram per liter of fluoride ion and 9.3 grams per liter of chloride ion.
  • Example 1-7 concentrations of the various ions in the solutions of Examples 1-7, together with some additional solutions according to this invention and four control solutions (Examples 10-13) not of this invention which are included for the sake of comparison in performance tests as described hereinafter. All concentrations are in grams per liter except for total acid and free acid, which are given in points as defined hereinabove.
  • Hydrofluoric acid added to provide 0.3 gram per liter of fluoride, all of which precipitated as calcium fluoride.
  • the metal surface is usually cleaned by physical and/ or chemical means to remove any grease, dirt and oxides.
  • the chemical cleaning step include a titanium phosphate pretreatment of the type disclosed in US. Pat. 2,322,349; such a pretreatment promotes formation of a microcrystalline coating as described hereinafter.
  • the cleaned article is then rinsed with water and treat ed with the phosphating solution.
  • the phosphating treatment may be by any of the commonly used techniques such as spraying, brushing, dipping, roller-coating and flow-coating.
  • the temperature of the phosphating solution may vary from about room temperature to about 240 F.; the solutions of the present invention are conveniently used at about 150180 F. and preferably about 160-165 F.
  • the phosphating operation is carried out until a phosphate coating of the desired weight is obtained; this weight may be as little as 25 mg. per square foot of surface area but is preferably about 50-1000 and .generally not more than about 300 mg. per square foot. Under most conditions, a coating within this weight range can be obtained when the duration of phosphate treating is between about seconds and minutes.
  • the metal article Upon completion of the phosphating operation, the metal article is generally rinsed with water and/ or a hot, dilute aqueous solution of chromic acid.
  • the chromic acid rinse appears to seal" the phosphate coating and improve its utility as a base for the application of a paint or other siccative organic coating.
  • a dilute aqueous solution of a metal chromate or dichromate, a chromic acid-phosphoric acid mixture, or a mixture of chromic acid with a metal dichromate may be used in place of the aqueous chromic acid.
  • solutions containing partially reduced chromic acid such as those described in US. Pats. 3,282,- 744 and 3,404,045.
  • compositions of this invention for forming phosphate coatings on both ferrous metals and zinc surfaces is believed to result in part from the crystalline structure of the coating formed.
  • Most of the previously known phosphating solutions form coatings with either an apatite or scholzite crystal structure.
  • the apatite structure is represented by (M (OH) (PO and scholzite by (M (M (POQ ZH O.
  • M (OH) (PO and scholzite by (M (M (POQ ZH O.
  • M and M in these formulas will depend on the metal ions present in the coating bath.
  • a phosphate bath containing zinc ions will produce an apatite-like coating wherein M is zinc.
  • a phosphate solution containing zinc and calcium ions such as that disclosed and claimed in US. Pat.
  • compositions of this invention produce a phosphate coating which, prior to drying, has predominantly a modified hopeite structure.
  • Hopeite has the formula Zn (PO -4H O.
  • An ordinary hopeite crystalline coating is deposited on a metal surface and dried, it loses water of hydration at low temperatures and becomes loose and nonadherent.
  • the compositions of this invention produce hopeite crystals with partial substitution (generally up to about 20%) of magnesium for zinc.
  • the presence of magnesium causes a change in the kinetics of drying so that the crystals lose only half their water of hydration, whereupon they are converted to thin needles which aggregate into thin bundles of parallel needles with strong epitaxial bonds to the metal surface.
  • the dehydrated crystals are very small, generally microcrystalline.
  • compositions of this invention for forming phosphate coatings on metal is demonstrated by the Salt Fog Corrosion Test (ASTM B117) and the Detergent Test. In these tests, cold-rolled steel and galvanized steel test :panels are cleaned at 160-165 F. with a cleaner of the following constitution:
  • Anhydrous sodium metasilicate 51 Anhydrous sodium metasilicate 51.
  • the paint film on each panel is ruptured down to the bare metal by scoring a six inch line on the surface of the panel.
  • the score panel is 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 remain in this atmosphere for 120 hours after which they are removed, washed with water and dried With a cloth. A pressuresensitive tape is then applied to each panel and removed suddenly. This procedure is repeated until no more paint can be removed in this manner. The loss of adhesion caused by corrosion from the scribed line is measured in thirty-seconds of an inch.
  • the painted panels are immersed in a 1% synthetic detergent solution at F. for the desired period, and are then removed and rated for blister size and frequency of blistering according to ASTM procedure B714.
  • the blister size is reported as a number from -0 to 10, 0 representing large blisters and 10 mp resenting no blistering.
  • the frequency of blistering is designated as dense, medium dense, medium or few.
  • Table II show the superiority of the compositions of this invention for forming phosphate coatings on both steel and galvanized surfaces, as compared with known calcium-modified zinc phosphate solutions.
  • An aqueous solution suitable for producing a microcrystalline coating on both zinc and ferrous metal surfaces, containing as essential coating-producing ingredients the following ions in the indicated concentrations: (A) Phosphate-3-20 grams per liter (B) Zinc-0.5-3.0 grams per liter (C) Nickel, cobalt or copper0.05-3.0, 0.0030.7 or
  • component C is nickel ion.
  • A Phosphate-3-15 grams per liter
  • B Zinc0.5-3.0 grams per liter
  • C Nickel0.l3.0 grams per liter
  • D Magnesium2.56.0 grams per liter
  • E Nitrite-0.010.25 gram per liter
  • F Fluoride and/or chloride-0.1-1.0 and 7-15 grams per liter, respectively.
  • a solution according to claim 3 which additionally contains nitrate ion in an amount up to about 40 grams per liter.
  • component F is fluoride ion.
  • component F is at least partially chloride ion.
  • a method of producing a microcrystalline phosphate coating on a ferrous meal or zinc surface which comprises contacting said surface with a solution according to claim 1.
  • a method of producing a microcrystalline phosphate coating on a ferrous metal or zinc surface which comprises contacting said surface with a solution according to claim 3.
  • component F is fluoride and the solution additionally contains nitrate ion in an amount up to about 40 grams per liter.
  • component F is at least partially chloride ion.
  • a ferrous metal or galvanized article which con tains on its surface a microcrystalline phosphate coating prepared by the method of claim 9.
  • a metal article according to claim 13 which has been further provided with a siccative organic coating.
  • a ferrous metal or galvanized article which contains on its surface a microcrystalline phosphate coating prepared by the method of claim 10.
  • a metal article according to claim 15 which has been further provided with a siccative organic coating.

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  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
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  • Chemical Treatment Of Metals (AREA)
US864875A 1969-10-08 1969-10-08 Phosphating solutions for use on ferrous metal and zinc surfaces Expired - Lifetime US3597283A (en)

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JP (1) JPS5014223B1 (de)
CA (1) CA929448A (de)
DE (1) DE2049350A1 (de)
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4053328A (en) * 1974-08-30 1977-10-11 Nippon Paint Co., Ltd. Zinc phosphate coating process
US4110128A (en) * 1975-12-17 1978-08-29 International Lead Zinc Research Organization, Inc. Solution and procedure for depositing a protective coating on galvanized steel parts, and solution regeneration procedure
US4110127A (en) * 1974-01-23 1978-08-29 International Lead Zinc Research Organization, Inc. Procedure for depositing a protective precoating on surfaces of zinc-coated ferrous metal parts against corrosion in presence of water
DE3004927A1 (de) * 1979-02-13 1980-08-21 Nippon Paint Co Ltd Verfahren zur phosphatierung von metallen
US4265677A (en) * 1979-02-23 1981-05-05 Oxy Metal Industries Corporation Phosphatizing prior to cathodic electropainting
EP0038122A1 (de) * 1980-03-19 1981-10-21 Amchem Products, Inc. Bildung korrosionsbeständiger Beschichtungen auf Metall-, insbesondere Zinkoberflächen
US4596607A (en) * 1985-07-01 1986-06-24 Ford Motor Company Alkaline resistant manganese-nickel-zinc phosphate conversion coatings and method of application
US4681641A (en) * 1982-07-12 1987-07-21 Ford Motor Company Alkaline resistant phosphate conversion coatings
US20030230364A1 (en) * 2002-04-29 2003-12-18 Greene Jeffrey Allen Conversion coatings including alkaline earth metal fluoride complexes
WO2004011231A1 (ja) * 2002-07-31 2004-02-05 Nippon Steel Corporation 樹脂ライニング鋼管およびその製造方法
US20090242080A1 (en) * 2006-10-31 2009-10-01 Satoru Ando Phosphate-treated galvanized steel sheet and method for making the same
WO2019006676A1 (zh) * 2017-07-04 2019-01-10 深圳市长宏泰科技有限公司 除油除锈磷化三合一皮膜剂、钢铁件及其皮膜化处理方法
WO2024149790A1 (en) * 2023-01-11 2024-07-18 Chemetall Gmbh Composition for phosphatizing of ferrous surfaces and method making use thereof

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JPS5811514B2 (ja) * 1979-05-02 1983-03-03 日本ペイント株式会社 金属表面の保護方法
DE3118375A1 (de) * 1981-05-09 1982-11-25 Metallgesellschaft Ag, 6000 Frankfurt Verfahren zur phosphatierung von metallen sowie dessen anwendung zur vorbehandlung fuer die elektrotauchlackierung
BR8208086A (pt) * 1982-07-12 1984-07-17 Ford Motor Co Processo para aumentar a resistencia a dissolucao alcalina de um revestimento de conversao de fosfato em um substrato de metal corrosivel,processo para revestir uma pelicula de fosfato sobre a superficie de um artigo de metal limpo por alcali,processo para aplicacao de um sistema de revestimento resistente a corrosao,e produto resultante
WO1985003089A1 (en) * 1984-01-06 1985-07-18 Ford Motor Company Alkaline resistance phosphate conversion coatings
JPS63100185A (ja) * 1986-10-16 1988-05-02 Nippon Parkerizing Co Ltd 冷延鋼板または亜鉛めっき鋼板のりん酸塩化成処理方法
ES2036666T3 (es) * 1987-08-19 1993-06-01 Metallgesellschaft Ag Procedimiento para fosfatar metales.
DE3828676A1 (de) * 1988-08-24 1990-03-01 Metallgesellschaft Ag Phosphatierverfahren
JPH03107469A (ja) * 1989-09-21 1991-05-07 Nippon Parkerizing Co Ltd 裸耐食性に優れたりん酸塩化成皮膜を有する亜鉛系めっき材料
DE4214992A1 (de) * 1992-05-06 1993-11-11 Henkel Kgaa Kupfer enthaltendes, nickelfreies Phosphatierverfahren
DE69326021T2 (de) * 1992-12-22 1999-12-23 Henkel Corp., Plymouth Meeting Im wesentlichen nickelfreier phosphatkonversionsüberzug-zusammensetzung und verfahren
US6070460A (en) * 1996-03-08 2000-06-06 Alliedsignal Inc. Apparatus and method for determining wind profiles and for predicting clear air turbulence
DE60044678D1 (de) * 1999-05-27 2010-08-26 Nippon Steel Corp Verfahren zur herstellung eines phosphatbehandelten elektrogalvanisierten stahlblechs mit ausgezeichneter korrosionsbeständigkeit und eignung zur beschichtung
KR100665467B1 (ko) * 1999-08-09 2007-01-04 신닛뽄세이테쯔 카부시키카이샤 가공성이 우수한 인산염 처리 아연계 도금 강판 및 그제조방법

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4110127A (en) * 1974-01-23 1978-08-29 International Lead Zinc Research Organization, Inc. Procedure for depositing a protective precoating on surfaces of zinc-coated ferrous metal parts against corrosion in presence of water
US4126469A (en) * 1974-01-23 1978-11-21 International Lead Zinc Research Organization, Inc. Solution and procedure for depositing a protective precoating on surfaces of zinc-coated ferrous metal parts against corrosion in presence of water
US4053328A (en) * 1974-08-30 1977-10-11 Nippon Paint Co., Ltd. Zinc phosphate coating process
US4110128A (en) * 1975-12-17 1978-08-29 International Lead Zinc Research Organization, Inc. Solution and procedure for depositing a protective coating on galvanized steel parts, and solution regeneration procedure
DE3004927A1 (de) * 1979-02-13 1980-08-21 Nippon Paint Co Ltd Verfahren zur phosphatierung von metallen
US4292096A (en) * 1979-02-13 1981-09-29 Nippon Paint Co., Ltd. Phosphating process of metal surface
US4265677A (en) * 1979-02-23 1981-05-05 Oxy Metal Industries Corporation Phosphatizing prior to cathodic electropainting
EP0038122A1 (de) * 1980-03-19 1981-10-21 Amchem Products, Inc. Bildung korrosionsbeständiger Beschichtungen auf Metall-, insbesondere Zinkoberflächen
US4681641A (en) * 1982-07-12 1987-07-21 Ford Motor Company Alkaline resistant phosphate conversion coatings
US4596607A (en) * 1985-07-01 1986-06-24 Ford Motor Company Alkaline resistant manganese-nickel-zinc phosphate conversion coatings and method of application
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DE2049350A1 (de) 1971-04-15
GB1288103A (de) 1972-09-06
CA929448A (en) 1973-07-03
JPS5014223B1 (de) 1975-05-26
FR2065066A5 (de) 1971-07-23

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