US2132883A - Method of coating ferrous metal with a water insoluble metallic phosphate - Google Patents
Method of coating ferrous metal with a water insoluble metallic phosphate Download PDFInfo
- Publication number
- US2132883A US2132883A US139947A US13994737A US2132883A US 2132883 A US2132883 A US 2132883A US 139947 A US139947 A US 139947A US 13994737 A US13994737 A US 13994737A US 2132883 A US2132883 A US 2132883A
- Authority
- US
- United States
- Prior art keywords
- solution
- coating
- phosphate
- zinc
- iron
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000576 coating method Methods 0.000 title description 60
- 239000011248 coating agent Substances 0.000 title description 48
- 238000000034 method Methods 0.000 title description 47
- 229910052751 metal Inorganic materials 0.000 title description 23
- 239000002184 metal Substances 0.000 title description 23
- 229910019142 PO4 Inorganic materials 0.000 title description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title description 19
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title description 18
- 239000010452 phosphate Substances 0.000 title description 18
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 title description 12
- 239000000243 solution Substances 0.000 description 140
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 54
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 27
- 229910052742 iron Inorganic materials 0.000 description 27
- 239000011701 zinc Substances 0.000 description 27
- 229910052725 zinc Inorganic materials 0.000 description 27
- 239000000126 substance Substances 0.000 description 22
- 238000005507 spraying Methods 0.000 description 20
- 230000008569 process Effects 0.000 description 19
- 235000021317 phosphate Nutrition 0.000 description 18
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 18
- LRXTYHSAJDENHV-UHFFFAOYSA-H zinc phosphate Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LRXTYHSAJDENHV-UHFFFAOYSA-H 0.000 description 16
- 229910000165 zinc phosphate Inorganic materials 0.000 description 15
- 229910000831 Steel Inorganic materials 0.000 description 11
- 230000001105 regulatory effect Effects 0.000 description 11
- 239000010959 steel Substances 0.000 description 11
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 9
- 150000003839 salts Chemical class 0.000 description 9
- 235000010288 sodium nitrite Nutrition 0.000 description 9
- CPSYWNLKRDURMG-UHFFFAOYSA-L hydron;manganese(2+);phosphate Chemical compound [Mn+2].OP([O-])([O-])=O CPSYWNLKRDURMG-UHFFFAOYSA-L 0.000 description 8
- 238000001556 precipitation Methods 0.000 description 7
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 6
- 230000009471 action Effects 0.000 description 6
- 238000007792 addition Methods 0.000 description 6
- 238000013019 agitation Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 6
- 229910052748 manganese Inorganic materials 0.000 description 6
- 239000011572 manganese Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 4
- 239000011260 aqueous acid Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 238000012937 correction Methods 0.000 description 4
- 239000004519 grease Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 3
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000001376 precipitating effect Effects 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 230000001680 brushing effect Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000003042 antagnostic effect Effects 0.000 description 1
- GJTDJAPHKDIQIQ-UHFFFAOYSA-L barium(2+);dinitrite Chemical compound [Ba+2].[O-]N=O.[O-]N=O GJTDJAPHKDIQIQ-UHFFFAOYSA-L 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229940116007 ferrous phosphate Drugs 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910000155 iron(II) phosphate Inorganic materials 0.000 description 1
- SDEKDNPYZOERBP-UHFFFAOYSA-H iron(ii) phosphate Chemical compound [Fe+2].[Fe+2].[Fe+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O SDEKDNPYZOERBP-UHFFFAOYSA-H 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- XMWCXZJXESXBBY-UHFFFAOYSA-L manganese(ii) carbonate Chemical compound [Mn+2].[O-]C([O-])=O XMWCXZJXESXBBY-UHFFFAOYSA-L 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910000403 monosodium phosphate Inorganic materials 0.000 description 1
- 235000019799 monosodium phosphate Nutrition 0.000 description 1
- -1 nitrates Chemical compound 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- RAFRTSDUWORDLA-UHFFFAOYSA-N phenyl 3-chloropropanoate Chemical compound ClCCC(=O)OC1=CC=CC=C1 RAFRTSDUWORDLA-UHFFFAOYSA-N 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000000276 potassium ferrocyanide Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- AJPJDKMHJJGVTQ-UHFFFAOYSA-M sodium dihydrogen phosphate Chemical compound [Na+].OP(O)([O-])=O AJPJDKMHJJGVTQ-UHFFFAOYSA-M 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- XOGGUFAVLNCTRS-UHFFFAOYSA-N tetrapotassium;iron(2+);hexacyanide Chemical compound [K+].[K+].[K+].[K+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] XOGGUFAVLNCTRS-UHFFFAOYSA-N 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000012224 working solution Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
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
- C23C22/73—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 characterised by the process
- C23C22/76—Applying the liquid by spraying
Definitions
- This invention relates to the art of applylns phosphate coatings to the surface of iron or steel, and particularly to the art of producing these coatings on a succession of pieces by treating them with an aqueous acid phosphate solution such, for example, as zinc phosphate.
- the solution employed in the process of the present invention may comprise a phosphate of a metal such as zinc or manganese.
- a phosphate of a metal such as zinc or manganese.
- I prefer to use zinc phosphate because of its more ready availability and relatively lower cost. Therefore, in the following description, I will refer to zinc phosphate, although it is to be understood that the same principles may very well be applied to other metals of a similar nature.
- the process in its preferred form, comprises subjecting a succession of iron or steel pieces serially to the action of an aqueous zinc phosphate solution, while substantially continuously adding to the solution, regulated quantities of the zinc phosphate solution and of a water solution of a salt of nitrous acid, which additions are made in an amount which is slimcient to maintain the metal content and the pH of the solution substantially constant and also substantially free of dissolved iron.
- the hot solution is supersaturated with respect to the zinc phosphate which precipitates.
- the solution rises in hydrogen ion concentration (falls in pH) due to the greater proportionate loss of zinc. This action continues until the solution has again reached equilibrium at the elevated temperature.
- the highest coating speed is likewise favored by elevation of temperature, up to the boiling point, and for best results the temperature of the solution should be quite accurately controlled.
- elevated temperatures have a tendency to cause the solution to lose its supersaturation, for which reason I prefer a temperature somewhere between F. and F., because my experience has shown that a temperature within this range will yield coatings in a period which is sumciently brief without causing the extremely rapid loss of supersaturation which occurs at higher temperatures.
- Violent agitation of the solution tends to speed up somewhat the rate at which it loses its supersaturation and falls in pH. Nevertheless, rapid renewal of the film of solution actually in contact with the surface of the metal, and the more or less violent agitation which it necessitates, is
- the removal of the iron from the solution may be effected in a number of ways, such, for example, as by the addition to the solution of chemicals capable of precipitating the ferrous iron or of oxidizing the ferrous iron to ferric iron, the latter being practically insoluble in the solution. Furthermore, adequate aeration of the solution may also be employed in removing the iron. I prefer, however, to precipitate the iron by adding a suitable chemical, and the chemical I employ has an added function which will be described below.
- the solution is capable of operating successfully at a given pH over a considerable range of zinc concentrations, but at a given zinc concentration the solution operates correctly only within a narrow pH band. Too high a pH, in general, causes useless precipitation of zinc phosphate, while too low a pH causes the process to become inoperative.
- the precipitating agent which I prefer to employ is a salt of nitrous acid, because such material will function not only as a medium for converting ferrous iron into insoluble ferric iron, but also as an agent for maintaining the pH of the solution substantially constant.
- Sodium nitrite is particularly suitable for the purpose, and I prefer to introduce it as a freshly prepared water solution.
- Barium nitrite or calcium nitrite may also be employed, or some other water soluble salt of nitrous acid.
- stampings as they come from the press, are generally contaminated with oil, grease, and/or drawing compound, and sometimes with rust. Unless the rusting is severe, the parts may be satisfactorily coated without removal of the rust. If severely rusted, the parts may be subjected to pickling or other de-rustlng treatment before entering the cleaning and coating system to be described.
- Grease, etc. should be removed from the articles to be coated by my process. This may be accomplished by any of the well-known conventional means such as wiping or washing with a solvent, vapor degreasing, or alkaline cleaning.
- the stampings After being properly cleaned and prepared for the coating operation, the stampings are subjected to a coating solution such, for example, as the following:
- the diluted solution is placed in a suitable tank which is preferably equipped with means for controlling the temperature of the solution.
- the temperature may vary considerably, but I have found that a temperature in the neighborhood of F. will produce excellent results.
- the above solution has an initial pH of about 2.5.
- any suitable spraying equipment may be provided, the details of which are not illustrated, because they may take various forms, dependent upon individual requirements.
- Circulation of the solution through the tanks to the spraying nozzles or jets is preferably provided for by means of a centrifugal pump, and the material which runs down from the work is collected in suitable troughs and returned to the tank or reservoir from which the solution is pumped.
- stampings to be coated are subjected to the impinging action of the jets of solution at a rate such as will provide for a treatment of from thirty seconds to one minute, although this period may vary considerably, depending upon conditions and the temperature of the solution.
- the pumping system is kept in continuous operation in order to provide for continuous circulation of the solution from the tank to the impinging nozzles or Jets, and from the jets to the work, and then back again to the tank.
- I immediately add to the solution regulated quantitles of the solution of Formula No. l, and also of a water solution of a. salt of nitrous acid, preferably sodium nitrite. These additions are made preferably at a point where the solution is in more or less violent agitation so as to insure thorough mixing with the body of the solution.
- the rate at which these solutions are introduced is regulated so as to maintain the zinc content and the pH of the coating solution substantially constant and also substantially freed of dissolved iron.
- the rate at which these solutions are introduced is regulated so as to maintain the zinc content and the pH of the coating solution substantially constant and also substantially freed of dissolved iron.
- To this and suitable determinations of the zinc content and of the pH may be made in any desired manner known to this art.
- the zinc content of the solution may be determined electrolytically or chemically.
- a convenient method consists in titrating a small sample of the solution with standard potassium ferrocyanide in accordance with the directions given in standard chemical text books.
- the pH may be determined colorimetrically or potentiometrically by any standard method.
- the potential of the glass electrode vs. a saturated calomel electrode furnishes a convenient measure of the pH of the solution.
- the zinc content of the solution may be varied over a considerable range without appreciably affecting the operation of the process, but for each zinc concentration there exists an optimum pH from which only narrow departures are allowable.
- the minimum pH (maximum hydrogen ion concentration) which is allowable to secure good coatings in the time allowable, varies a little with the type of metal to be coated, and the method of cleaning employed.
- the correct pH likewise varies with the temperature at which the coating solution is maintained.
- F'or solvent-cleaned steel values about 0.1 pH unit lower my be used to obtain excellent coatings.
- my experience has shown that a solution which operates perfectly with alkalicleaned steel will likewise operate perfectly with solvent cleaned steel, if both are reasonably free of grease and uniformly cleaned.
- stampings After the stampings have been coated they may be washed and then dried, whereupon they are ready for the application of any desired finish, such as paint, varnish, lacquer, Japan, or the like.
- the zinc restoring solution may be the concentrated solution of Formula No. l, and the sodium nitrite solution may contain about 60 grams of sodium nitrite per liter of water.
- the zinc-containing solution used for maintaining the zinc concentration of the coating solution may likewise be varied considerably in composition and in concentration. It is convenient, however, to use the same solution as was originally used for making up the original coating solution.
- the pH and the manganese content of the coating solution are maintained constant at appropriate values in a manner entirely analogous to the maintenance of the pH and the zinc content of the coating solution of the given example.
- the content of coating metal in the Working solution is determined by standard chemical methods forming no part of the present invention. Rapid methods of chemical analysis, such as titrations, are naturally to be preferred.
- My improved process is capable of giving the finest-grained and smoothest coatings on surfaces which have been alkali-cleaned and rinsed, without drying, wiping, brushing or mechanical treatment either prior to or during the coating operation, which is a distinct and marked advantage over previous processes known to me, which, for the production of the smoothest coating, require that the work be solvent-cleaned and wiped or brushed before coating, or, at least, if it be alkalicleaned, that it be dried and solvent-wiped before being coated, or that it be mechanically rubbed during the coating operation.
- This advantage makes it possible to combine the apparatus stages, in which the pre-cleaning is performed, into one continuous unit with the coating stage, which, of course, effects a corresponding saving in floor space and a marked economy in construction and equipment costs.
- the substantially continuously operable method which comprises spraying a succession of pieces with a zinc phosphate solution; collecting the run-oil for re-use in the spraying operation; and substantially continuously adding to the solution regulated quantities of zinc phosphate and of a soluble salt of nitrous acid suflicient to maintain the sprayed solution substantially constant as to zinc content and pH and also substantially free of dissolved iron.
- substantially continuously operable method which comprises spraying a succession of pieces with a zinc phosphate solution; collecting the runof! for re-use in the spraying operation; and substantially continuously adding to the solution regulated quantities of zinc phosphate solution and of an aqueous solution of sodium nitrite suflicient to maintain the sprayed solution sub stantially constant as to zinc content and pH and also substantially free of dissolved iron.
- the substantially continuously operable method which includes spraying a succession of pieces with an aqueous acid phosphate coating solution which is substantially free of dissolved iron, collecting the run-off for re-use in the spraying operation, and substantially continuously adding to the solution regulated quantities of the acid phosphate and of a soluble salt of nitrous acid sufficient to maintain the sprayed solution substantially constant as to its metal content and pH and also substantially free of dissolved iron.
- the substantially continuously operable method which includes spraying a succession of pieces with an aqueous acid phosphate coating solution which is substantially free of dissolved iron, collecting the run-off for re-use in the spraying operation, and substantially continuously adding to the solution regulated quantities of aqueous acid phosphate coating solution and of a water solution of a salt of nitrous acid sufficient to maintain the sprayed solution substantially constant as to its metal content and pH and also substantially free of dissolved iron.
- the substantially continuously operable method which comprises spraying a succession of pieces with a manganese phosphate solution; collecting the run-01f for re-use in the spraying operation; and substantially continuously adding to the solution regulated quantities oi manganese phosphate and of a soluble salt of nitrous acid sufficient to maintain the sprayed solution substantially constant as to manganese content and pH and also substantially free of dissolved iron.
- the substantially continuously operable method which comprises spraying a succession of pieces with a manganese phosphate solution; collecting the run-oflf for re-use in the spraying operation, and substantially continuously adding to the solution regulated quantities of manganese phosphate solution and of an aqueous solution of sodium nitrite sufficient to maintain the sprayed solution substantially constant as to manganese content and pH and also substantially free of dissolved iron.
- the substantially continuously operable method which comprises spraying a succession of pieces with a manganese phosphate solution; collecting the run-01f for re-use in the spraying operation; and substantially continuously adding to the solution regulated quantities oi manganese phosphate and of a soluble salt of nitrous acid sufficient to maintain the sprayed solution substantially constant as to manganese content and pH and also substantially free of dissolved iron.
- the substantially continuously operable method which comprises spraying a succession of pieces with a manganese phosphate solution; collecting the run-oflf for re-use in the spraying operation, and substantially continuously adding to the solution regulated quantities of manganese phosphate solution and of an aqueous solution of sodium nitrite sufficient to maintain the sprayed solution substantially constant as to manganese content and pH and also substantially free of dissolved iron.
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- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Treatment Of Metals (AREA)
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DENDAT863889D DE863889C (de) | 1937-04-30 | Verfahren zur Erzeugung von Phosphatschichten auf Metallen | |
BE427074D BE427074A (en(2012)) | 1937-04-30 | ||
US139947A US2132883A (en) | 1937-04-30 | 1937-04-30 | Method of coating ferrous metal with a water insoluble metallic phosphate |
GB23669/37A GB501739A (en(2012)) | 1937-04-30 | 1937-08-30 | |
FR847128D FR847128A (fr) | 1937-04-30 | 1938-04-30 | Procédé pour la production de revêtements phosphatés sur des métaux |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US139947A US2132883A (en) | 1937-04-30 | 1937-04-30 | Method of coating ferrous metal with a water insoluble metallic phosphate |
Publications (1)
Publication Number | Publication Date |
---|---|
US2132883A true US2132883A (en) | 1938-10-11 |
Family
ID=22489025
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US139947A Expired - Lifetime US2132883A (en) | 1937-04-30 | 1937-04-30 | Method of coating ferrous metal with a water insoluble metallic phosphate |
Country Status (5)
Country | Link |
---|---|
US (1) | US2132883A (en(2012)) |
BE (1) | BE427074A (en(2012)) |
DE (1) | DE863889C (en(2012)) |
FR (1) | FR847128A (en(2012)) |
GB (1) | GB501739A (en(2012)) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE741937C (de) * | 1941-03-11 | 1943-11-20 | Metallgesellschaft Ag | Verfahren zur Herstellung von Phosphatueberzuegen auf Metallen |
US2479423A (en) * | 1946-02-07 | 1949-08-16 | American Chem Paint Co | Method of and materials for treating surfaces of iron, zinc, and alloys of each |
DE753259C (de) * | 1940-03-04 | 1952-07-14 | American Chem Paint Co | Verfahren zur Erzeugung von Phosphatschichten |
US2609308A (en) * | 1947-11-22 | 1952-09-02 | Parker Rust Proof Co | Method and material for producing coatings on metal |
US2743204A (en) * | 1952-08-28 | 1956-04-24 | Parker Rust Proof Co | Phosphate metal coatings |
DE1181520B (de) * | 1959-07-09 | 1964-11-12 | Agep Gnacke & Co Chem Fab | Verfahren zur Schutzschichtbildung auf Metallen oder Metallegierungen |
US3178320A (en) * | 1960-07-29 | 1965-04-13 | John A Henricks | Method and composition for the formation of smooth zinc phosphate coatings on steel |
US3874951A (en) * | 1972-09-27 | 1975-04-01 | Trw Inc | Method for controlling iron content of a zinc phosphating bath |
US4086103A (en) * | 1975-08-13 | 1978-04-25 | Kevin James Woods | Accelerator for phosphating solutions |
US4186219A (en) * | 1975-08-29 | 1980-01-29 | Union Carbide Corporation | Maintaining the effectiveness of a coating composition |
US4233088A (en) * | 1979-03-29 | 1980-11-11 | International Lead Zinc Research Organization, Inc. | Phosphatization of steel surfaces and metal-coated surfaces |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1046440B (de) * | 1952-06-03 | 1958-12-11 | Exxon Research Engineering Co | Korrosionsschutzmittel und Verfahren zum Schutz eisenhaltiger Flaechen |
-
0
- DE DENDAT863889D patent/DE863889C/de not_active Expired
- BE BE427074D patent/BE427074A/xx unknown
-
1937
- 1937-04-30 US US139947A patent/US2132883A/en not_active Expired - Lifetime
- 1937-08-30 GB GB23669/37A patent/GB501739A/en not_active Expired
-
1938
- 1938-04-30 FR FR847128D patent/FR847128A/fr not_active Expired
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE753259C (de) * | 1940-03-04 | 1952-07-14 | American Chem Paint Co | Verfahren zur Erzeugung von Phosphatschichten |
DE741937C (de) * | 1941-03-11 | 1943-11-20 | Metallgesellschaft Ag | Verfahren zur Herstellung von Phosphatueberzuegen auf Metallen |
US2479423A (en) * | 1946-02-07 | 1949-08-16 | American Chem Paint Co | Method of and materials for treating surfaces of iron, zinc, and alloys of each |
US2609308A (en) * | 1947-11-22 | 1952-09-02 | Parker Rust Proof Co | Method and material for producing coatings on metal |
US2743204A (en) * | 1952-08-28 | 1956-04-24 | Parker Rust Proof Co | Phosphate metal coatings |
DE1181520B (de) * | 1959-07-09 | 1964-11-12 | Agep Gnacke & Co Chem Fab | Verfahren zur Schutzschichtbildung auf Metallen oder Metallegierungen |
US3178320A (en) * | 1960-07-29 | 1965-04-13 | John A Henricks | Method and composition for the formation of smooth zinc phosphate coatings on steel |
US3874951A (en) * | 1972-09-27 | 1975-04-01 | Trw Inc | Method for controlling iron content of a zinc phosphating bath |
US4086103A (en) * | 1975-08-13 | 1978-04-25 | Kevin James Woods | Accelerator for phosphating solutions |
US4186219A (en) * | 1975-08-29 | 1980-01-29 | Union Carbide Corporation | Maintaining the effectiveness of a coating composition |
US4233088A (en) * | 1979-03-29 | 1980-11-11 | International Lead Zinc Research Organization, Inc. | Phosphatization of steel surfaces and metal-coated surfaces |
Also Published As
Publication number | Publication date |
---|---|
DE863889C (de) | 1952-12-04 |
BE427074A (en(2012)) | |
GB501739A (en(2012)) | 1939-02-28 |
FR847128A (fr) | 1939-10-03 |
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